JPH08183890A - Thermoplastic resin composition - Google Patents

Abstract

PURPOSE: To obtain a thermoplastic resin composition containing a maleimide copolymer and an ABS resin and having high heat resistance, high impact resistance and excellent moldability. CONSTITUTION: This composition comprises 5-50 pts.wt. maleimide copolymer (A) comprising aromatic vinyl monomer residues, unsaturated diarboxylic acid imide derivative residues and residues of vinyl monomers copolymerizable therewith, 0-50 pts.wt. vinyl-aromatic copolymer (B) comprising aromatic vinyl monomer residues, vinyl cyanide monomer residues and residues of vinyl monomers copolymerizable therewith, and 10-50 pts.wt. graft copolymer (C) prepared by grafting a mixture comprising an aromatic vinyl monomer, a vinyl cyanide monomer and vinyl monomers copolymerizable therewith onto a rubbery polymer [the total of components A to C being 100 pts.wt.] and has a residual metal content of 2000ppm or below.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a thermoplastic resin composition having excellent heat resistance, impact resistance and moldability. More specifically, it relates to a thermoplastic resin composition containing a maleimide copolymer having an unsaturated dicarboxylic acid imide derivative residue. The thermoplastic resin composition of the present invention can be preferably used for automobile parts, electric / electronic parts, office equipment parts, heat appliances, tableware, refrigerator parts, bath parts, shower parts, water purifier parts, toilet seats and the like.

[0002]

2. Description of the Related Art Conventionally, a method for producing a copolymer having an unsaturated dicarboxylic acid imide derivative residue has been known (US Pat. No. 3,840,499, US Pat. No. 39).
9907). However, although this maleimide-based copolymer has excellent heat resistance, it has extremely poor impact resistance and moldability.

Therefore, the maleimide-based copolymer has ABS
A resin composition in which a resin is blended to improve impact resistance is also known, but it is still inferior in impact resistance and molding processability and is not sufficient (US Pat. No. 3,642,949, US Pat. No. 3,652,726). , JP-A-57-9
No. 8536).

[0004]

That is, a resin having high heat resistance, high impact resistance and excellent molding processability has not yet been obtained by blending a maleimide copolymer with an ABS resin. At present, there is a strong demand for the development of a high-performance resin that also serves as a combination.

[Means for solving problems]

The inventors of the present invention have made extensive studies in order to solve the above-mentioned drawbacks of the resin composition of the maleimide copolymer and the ABS resin, and as a result, the maleimide copolymer of the component (A),
In the resin composition comprising the vinyl aromatic copolymer as the component (B) and the graft copolymer as the component (C), the heat resistance can be improved by adjusting the residual metal element content in the resin composition to 2000 ppm or less. It was found that a thermoplastic resin composition having excellent impact resistance and molding processability can be obtained, and the present invention has been achieved.

That is, the conventional ABS resin has no adverse effect on the physical properties even if the residual metal element content exceeds 2000 ppm, but the maleimide copolymer of the component (A) of the present invention,
It has been found that the thermoplastic resin composition comprising the vinyl aromatic copolymer as the component (B) and the graft copolymer as the component (C) has reduced impact resistance and moldability due to residual metal. As a result of diligent studies on the residual metal element, it was found that the impact resistance and the molding processability can be greatly improved by setting the residual metal element amount to 2000 ppm or less.

That is, the present invention relates to the component (A): an aromatic vinyl monomer residue, an unsaturated dicarboxylic acid imide derivative residue, and a maleimide copolymer consisting of a vinyl monomer residue copolymerizable therewith. 5 to 50 parts by weight of polymer, component (B):
Aromatic vinyl monomer residue, vinyl cyanide monomer residue,
And 0 to 50 parts by weight of a vinyl aromatic copolymer comprising a vinyl monomer residue copolymerizable therewith, a component (C): a rubber-like polymer, an aromatic vinyl monomer and a vinyl cyanide monomer. Graft copolymer 1 obtained by graft-polymerizing a monomer and a monomer mixture containing a vinyl monomer copolymerizable therewith
A resin composition consisting of 0 to 50 parts by weight (however, the total amount of the components (A), (B), and (C) is 100 parts by weight), and the amount of residual metal elements in the resin composition is 200
It is obtained by making the thermoplastic resin composition to be 0 ppm or less.

Hereinafter, the thermoplastic resin composition of the present invention will be described in detail. The maleimide copolymer as the component (A) contained in the thermoplastic resin composition of the present invention will be described. In producing the component (A), the first production method is an aromatic vinyl monomer, an unsaturated dicarboxylic acid imide derivative, an unsaturated dicarboxylic acid anhydride monomer and a vinyl monomer copolymerizable therewith. A method of copolymerizing the mixture,
The second method is to copolymerize an aromatic vinyl monomer, an unsaturated dicarboxylic acid anhydride monomer and a vinyl monomer mixture copolymerizable therewith, and then unsaturated the copolymer. Ammonia and / or first dicarboxylic acid anhydride group
Examples thereof include a method of reacting with a primary amine to convert to an imide group, and a maleimide copolymer can be obtained by any method.

Examples of the aromatic vinyl monomer constituting the component (A) include styrene-based monomers such as styrene, α-methylstyrene, vinyltoluene, t-butylstyrene and chlorostyrene and substituted monomers thereof. Of these, styrene is particularly preferred.

Examples of the unsaturated dicarboxylic acid imide derivative include maleimide, N-methylmaleimide, N-ethylmaleimide, N-cyclohexylmaleimide, N-phenylmaleimide and N-naphthylmaleimide. Of these, N-phenylmaleimide is preferable.

Examples of the unsaturated dicarboxylic acid anhydride monomer include anhydrides such as maleic acid, itaconic acid, citraconic acid and aconitic acid. Of these, maleic anhydride is particularly preferred.

Vinyl monomers copolymerizable with them include vinyl cyanide monomers such as acrylonitrile and methacrylonitrile, and acrylic acid ester monomers such as methyl acrylic acid ester, ethyl acrylic acid ester and butyl acrylic acid ester. Polymer, methyl methacrylate,
Examples thereof include methacrylic acid ester monomers such as ethyl methacrylic acid ester, vinylcarboxylic acid monomers such as acrylic acid and methacrylic acid, acrylic acid amides, methacrylic acid amides, and N-vinylcarbazole. Among these, monomers such as acrylic acid ester, methacrylic acid ester, acrylic acid and methacrylic acid are particularly preferable. Also,
The unsaturated dicarboxylic acid anhydride monomer is also mentioned as a copolymerizable vinyl monomer in the first production method, and is also used as the unsaturated dicarboxylic acid anhydride group remaining without being converted into an imide group in the second production method. It can be incorporated into the copolymer.

In the case of the first production method for producing the component (A), bulk-suspension polymerization, solution polymerization and bulk polymerization are carried out, and in the case of the second production method, suspension polymerization, emulsion polymerization, solution polymerization and bulk polymerization are carried out. A known polymerization method such as polymerization can be used.

The ammonia or the primary amine used in the imidization reaction to obtain the maleimide copolymer in the second production method may be in either anhydrous or aqueous solution. Examples of primary amines include alkylamines such as methylamine, ethylamine, cyclohexylamine, and /
Alternatively, aromatic amines such as aniline, toluidine, and naphthylamine can be used. Of these, aniline is particularly preferable.

When the imidation reaction is carried out in a solution state or a suspension state, it is preferable to use an ordinary reaction vessel, for example, an autoclave, and when it is carried out in a bulk molten state, an extruder equipped with a devolatilization device is used. May be.

The temperature of the imidization reaction is about 80 to 350 ° C, preferably 100 to 300 ° C. When the temperature is lower than 80 ° C, the reaction rate is slow and the reaction requires a long time, which is not practical. On the other hand, when the temperature exceeds 350 ° C, the physical properties are deteriorated due to thermal decomposition of the polymer. A catalyst may be used during the imidization reaction, and in this case, a tertiary amine such as triethylamine is preferably used.

Component (A) is an aromatic vinyl monomer residue,
It is a maleimide-based copolymer composed of an unsaturated dicarboxylic acid imide derivative residue and a vinyl monomer residue copolymerizable therewith, and the preferred aromatic vinyl monomer used as the component (A) is from 40 to It is 80% by weight, and if it is less than 40% by weight, the moldability is lowered, and if it exceeds 80% by weight, the heat resistance is lowered. The unsaturated dicarboxylic acid imide derivative residue is preferably 10 to 60% by weight, and 10% by weight
If it is less than 60% by weight, the heat resistance is not sufficiently improved, and if it exceeds 60% by weight, the impact resistance of the composition is significantly lowered. Further, the vinyl monomer residue copolymerizable with these is preferably 0 to 20.
%, And if it exceeds 20% by weight, the compatibility with the components (B) and (C) decreases, impact resistance also decreases, and delamination easily occurs.

The aromatic vinyl monomer used as the component (A) is preferably styrene, and the unsaturated dicarboxylic acid imide derivative is particularly preferably N-phenylmaleimide from the viewpoint of heat resistance. Further, as the aromatic vinyl monomer copolymerizable with these, maleic anhydride and acrylonitrile are particularly preferable.

Next, the vinyl aromatic copolymer as the component (B) will be described. The component (B) of the present invention is a vinyl aromatic copolymer comprising an aromatic vinyl monomer residue, a vinyl cyanide monomer residue, and a vinyl monomer residue copolymerizable therewith. . The component (B) is an aromatic vinyl monomer,
It can be produced by a usual polymerization method using a vinyl cyanide monomer and a vinyl monomer copolymerizable therewith, and for example, a polymerization method such as suspension polymerization, solution polymerization or emulsion polymerization can be adopted.

As the aromatic vinyl monomer, styrene,
It is a styrene-based monomer such as α-methylstyrene, vinyltoluene, t-butylstyrene and chlorostyrene, and styrene is particularly preferable. Examples of the vinyl cyanide monomer include acrylonitrile, methacrylonitrile, α-chloroacrylonitrile, etc., and acrylonitrile is particularly preferable. In addition, examples of vinyl monomers copolymerizable therewith include acrylic acid ester monomers such as methyl acrylic acid ester, ethyl acrylic acid ester and butyl acrylic acid ester, and methacrylic acid monomers such as methyl methacrylic acid ester and ethyl methacrylic acid ester. Acid ester monomer, vinylcarboxylic acid monomer such as acrylic acid and methacrylic acid, acrylic acid amide, methacrylic acid amide, and N
-Vinylcarbazol and the like can be mentioned. Among these, monomers such as acrylic acid ester, methacrylic acid ester, acrylic acid, and methacrylic acid are particularly preferable.

The preferred aromatic vinyl monomer residue in the component (B) is from 60 to 80% by weight. When it is less than 60% by weight, moldability is lowered, and when it exceeds 80% by weight, heat resistance is lowered. The preferred vinyl cyanide monomer residue is 20 to
It is 40% by weight, and if it is less than 20% by weight or more than 40% by weight, the compatibility with the component (A) is reduced, which causes delamination of the composition and reduction in impact strength. Further, a preferable vinyl monomer residue copolymerizable with these is 0 to 20% by weight,
If it exceeds 20% by weight, the compatibility with the components (A) and (C) decreases, the impact resistance also decreases, and layer delamination occurs.

Next, the graft copolymer as the component (C) will be described. The graft copolymer of the component (C) of the present invention is a monomer composed of an aromatic vinyl monomer, a vinyl cyanide monomer and a vinyl monomer copolymerizable therewith in the presence of a rubbery polymer. The body mixture is graft-polymerized.

The aromatic vinyl monomer used as the component (C) is a styrene-based monomer such as styrene, α-methylstyrene, vinyltoluene, t-butylstyrene and chlorostyrene, and styrene is particularly preferable. Examples of the vinyl cyanide monomer include acrylonitrile, methacrylonitrile, α-chloroacrylonitrile, etc., and acrylonitrile is particularly preferable.

The rubber-like polymer is a polymer composed of butadiene alone or a vinyl monomer copolymerizable therewith, or a polymer composed of an acrylic ester homopolymer or a vinyl monomer copolymerizable therewith. In the production of this graft copolymer, any known polymerization technique can be adopted, for example, aqueous heterogeneous polymerization such as suspension polymerization, emulsion polymerization, bulk polymerization, solution polymerization and in a poor solvent of the produced polymer. And the combination thereof.

In each component of the preferred component (C), the rubber-like polymer is 35 to 65 parts by weight. If it is less than 35 parts by weight, impact resistance is low, and if it exceeds 65 parts by weight, moldability and heat resistance are low. descend. Further, the preferred aromatic vinyl monomer in the monomer mixture is 50 to 80% by weight. If it is less than 50% by weight, moldability is deteriorated, and if it exceeds 80% by weight, impact resistance is deteriorated. Further, the preferred vinyl cyanide monomer is 20 to 40% by weight, and if it is less than 20% by weight or more than 40% by weight, the compatibility with the maleimide copolymer (A) is lowered and the impact resistance is remarkably increased. Get lower. The vinyl monomer copolymerizable with these is 0 to 30% by weight.

The rubber particle size is in the range of 0.1 to 0.6 μm,
It is preferable in terms of impact resistance. The graft ratio is 20-
When it is 80% and the weight average molecular weight of the ungrafted copolymer is in the range of 50,000 to 200,000, the impact resistance and the moldability are well balanced.

In the graft polymerization of the component (C) of the present invention, it is generally difficult to graft the entire amount of the monomer onto the rubber-like polymer, and an ungrafted copolymer is produced as a by-product. In the present invention, the true graft copolymer obtained by separating / removing the ungrafted copolymer is, needless to say, may be the graft polymer containing the ungrafted copolymer, and both should be treated as the graft copolymer. You can

Further, since it is important to reduce the amount of residual metal elements in the resin, not only the polymerization method but also the method of producing each of the components (A), (B) and (C) is required. It is necessary to pay close attention to the amount and type of catalyst, emulsifier, and precipitant used, and the method of precipitation.

A specific method for reducing the amount of residual metal elements to 2000 ppm or less is to use a precipitant containing no metal element such as sulfuric acid or hydrochloric acid as a precipitant. When a precipitant containing a metal element such as magnesium sulfate or calcium chloride is used, the amount of the metal compound such as magnesium sulfate or calcium chloride dissolved in the precipitant is 10 parts or less based on 100 parts of the polymer to be precipitated. There is a way to limit it to.

Further, the precipitated polymer is washed with water two or more times, or the precipitated wet cake is centrifuged.
It is also effective to filter under reduced pressure.

The component (A), the component (B) in the present invention,
The compounding ratio of the component (C) is 5 to 50 parts by weight of the component (A),
Component (B) is 0 to 50 parts by weight, component (C) is 10 to 50 parts by weight, and more preferable amounts are (A) component 10 to 45 parts by weight, (B) component 5 to 45 parts by weight and (C) component. 15-4
5 parts by weight and (A) component, (B) component, and (C)
The total amount of components is 100 parts by weight. Especially (A) component is 5
If it is less than part by weight, the heat resistance is not sufficient, and if it exceeds 50 parts by weight, the impact resistance and molding processability of the composition are significantly reduced. Further, if the component (B) exceeds 50 parts by weight, there is a problem that the heat resistance is lowered. If the amount of the component (C) is less than 10 parts by weight, the impact resistance will decrease, and if it exceeds 50 parts by weight, the heat resistance and the moldability will decrease.

The method of mixing the components (A) to (C) to obtain the thermoplastic resin composition of the present invention is not particularly limited,
Known means can be used. Examples of the means include a Banbury mixer, a tumbler mixer, a mixing roll, a single-screw or twin-screw extruder, and the like. As a mixing form, there are a method of obtaining a resin composition by ordinary contact mixing, multistage melt mixing using master pellets, blending in a solution, and the like.

The composition of the present invention may further contain stabilizers, flame retardants, plasticizers, lubricants, UV absorbers, colorants and talc,
It is also possible to add fillers such as silica, clay, mica and calcium carbonate.

The coloring agent can be usually used in ABS resin, and includes titanium oxide, iron oxide (valve), ultramarine blue, phthalocyanine blue, carbon black, titanium yellow, cobalt blue, perinone red, quinacridone red, anthraquinone red. Etc. are preferred.

The thermoplastic resin composition of the present invention is used in applications where heat resistance, impact resistance and molding processability are required. For example, door core materials for automobile parts, instrument panel cores, spoilers, pillar sunroof frames, defrosters. grill,
It is suitable for lamp housings, electric / electronic equipment parts, tableware, heat appliances, electric refrigerator parts, toilet seats, microwave oven parts, OA equipment parts, and industrial machine parts.

Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to the following Examples as long as the gist thereof is not exceeded. All parts and% in the examples and comparative examples are based on weight unless otherwise specified.

【Example】

Examples 1 to 10 and Comparative Examples 1 to 8 (1) Manufacture of component (A) (Manufacture of component (A) -1) 60 parts of styrene and 100 parts of methyl ethyl ketone were charged into an autoclave equipped with a stirrer to prepare a system. After replacing the inside with nitrogen gas, the temperature was raised to 85 ° C., and maleic anhydride 40
Parts and 0.15 parts of benzoyl peroxide in 200 parts of methyl ethyl ketone were continuously added over 8 hours. The temperature was kept at 85 ° C. for a further 3 hours after the addition. To the copolymer solution obtained here, 38 parts of aniline and 0.6 part of triethylamine were added and reacted at 140 ° C. for 7 hours. The reaction solution was supplied to a twin-screw extruder with a vent and devolatilized to obtain a maleimide-based copolymer. From C-13 NMR analysis, the conversion rate of acid anhydride groups to imide groups was 92 mol%. This maleimide copolymer was a copolymer containing 52% of N-phenylmaleimide units as an unsaturated dicarboxylic acid imide derivative, and this was designated as copolymer A-1.

Preparation of component (A) -2 In an autoclave equipped with a stirrer, 60 parts of styrene and 100 parts of methyl ethyl ketone were charged, the system was replaced with nitrogen gas, and the temperature was raised to 100 ° C. to keep the temperature. While stirring well. Methyl ethyl ketone 150
Polymerization was performed while continuously adding 40 parts of N-phenylmaleimide and 0.25 part of benzoylperoxide dissolved in 8 parts in 8 hours. After the completion of the polymerization, the reaction solution was supplied to a twin-screw extruder with a vent and dried to obtain a maleimide-based copolymer. According to C-13 NMR analysis, this copolymer was a copolymer containing 42% of N-phenylmaleimide units as an unsaturated dicarboxylic acid imide derivative. This was designated as copolymer A-2.

Preparation of component (A) -3 120 parts of pure water and sodium dodecylbenzene sulfonate (emulsifier) 2 in an autoclave equipped with a stirrer
Parts, styrene 54 parts, N-phenylmaleimide 34 parts,
Acrylonitrile 12 parts, sodium persulfate (initiator)
0.5 parts and t-dodecyl mercaptan (chain transfer agent) 0.5 parts were charged all at once, and the temperature was raised to 70 ° C. to carry out polymerization. After the polymerization, 300 parts of a 5% aqueous solution of magnesium sulfate was added to cause precipitation, followed by dehydration and drying to obtain a maleimide copolymer. From C-13 NMR analysis, this copolymer was a copolymer containing 33% of N-phenylmaleimide units as an unsaturated dicarboxylic acid imide derivative. This was designated as copolymer A-3. The composition analysis results of A-1 to A-3 are shown in Table-1.
Shown in

[0040]

[Table 1]

In the abbreviations in Table 1, St is styrene, NPMI is N-phenylmaleimide, MAH is maleic anhydride, and AN is acrylonitrile. The weight average molecular weight is a polystyrene-equivalent weight average molecular weight determined by GPC (gel permeation chromatography) measurement and by preparing a calibration curve using polystyrene having a standard molecular weight.

(2) Production of component (B) In a reaction can equipped with a stirrer, 70 parts of styrene, 30 parts of acrylonitrile, 2.5 parts of calcium triphosphate, 0.5 part of t-dodecyl mercaptan, and 0 part of benzoyl peroxide. .2 parts and 250 parts of water were charged and the temperature was raised to 70 ° C. to start polymerization. After 7 hours from the start of polymerization, the temperature was further increased to 7
The temperature was raised to 5 ° C. and kept for 3 hours to complete the polymerization. The polymerization rate reached 97%. 5% hydrochloric acid aqueous solution was added to the obtained reaction solution
0 part was added and precipitated, dehydrated and dried to obtain a white bead-shaped copolymer. This was designated as copolymer B-1. The copolymer was 70% styrene and 30% acrylonitrile.

(3) Production of component (C) Production of component (C) -1 Polybutadiene latex 1 in a reactor equipped with a stirrer
43 parts (solid content 35% weight average particle size 0.25 μm, gel content 90%), sodium stearate 1 part, sodium formaldehyde sulfoxylate 0.1 part, tetrasodium ethylenediamine tetraacetic acid 0.03
Parts, 0.003 parts of ferrous sulfate, and 150 parts of pure water are heated to a temperature of 50 ° C., and 50 parts of a monomer mixture consisting of 70% styrene and 30% acrylonitrile, 0.2 parts of t-dodecyl mercaptan. And 0.15 parts of Kyumen hydroperoxide were continuously added over 6 hours, and after the addition, the temperature was raised to 65 ° C. and polymerization was performed for 2 hours. The polymerization rate reached 97%. After adding an antioxidant to the obtained latex,
After adding 300 parts of a 5% calcium chloride aqueous solution, coagulation, washing with water and drying, a graft copolymer was obtained as a white powder. This was designated as copolymer C-1.

Preparation of component (C) -2 The same procedure as in graft copolymer C-1 was carried out until a latex was obtained. Furthermore, the same procedure as for the graft copolymer C-1 was carried out except that 100 parts of 5% calcium chloride aqueous solution and 200 parts of 5% hydrochloric acid aqueous solution were used instead of adding 300 parts of 5% calcium chloride aqueous solution to the obtained latex. The graft copolymer C-2 was obtained.

Preparation of component (C) -3 Preparation of graft copolymer C-1 except that 300 parts of 5% calcium chloride aqueous solution was replaced with 10 parts of 5% calcium chloride aqueous solution and 300 parts of 5% hydrochloric acid aqueous solution. This was carried out to obtain a graft copolymer C-3.

Preparation of component (C) -4 Graft copolymer C except that 300 parts of a 5% calcium chloride aqueous solution was replaced with 300 parts of a 5% magnesium sulfate aqueous solution.
An experiment was performed in the same manner as in -1, to obtain a graft copolymer C-4.

Preparation of component (C) -5 300 parts of 5% calcium chloride aqueous solution was added to 5% sulfuric acid aqueous solution 2
A graft copolymer C-5 was obtained in the same manner as in the graft copolymer C-1, except that the amount of the copolymer was changed to 00 parts and 100 parts of a 5% magnesium sulfate aqueous solution.

Preparation of Component (C) -6 The same procedure as in Graft Copolymer C-1 was conducted except that 300 parts of 5% calcium chloride aqueous solution was replaced with 300 parts of 5% zinc sulfate aqueous solution. -6 was obtained.

Preparation of component (C) -7 Preparation was carried out in the same manner as the graft copolymer C-1 except that 300 parts of 5% calcium chloride aqueous solution was replaced with 100 parts of 5% zinc sulfate aqueous solution and 200 parts of 5% sulfuric acid aqueous solution. Conducted to obtain a graft copolymer C-7.

Component (A), component (B), and component (C) are blended in the ratios shown in Tables 2 to 4, and the blended product is rotated in the same direction with a devolatilizer of 35 m / m in a biaxial direction. It was extruded using an extruder at a temperature of 250 ° C and pelletized. Using the pellets, an injection molding machine was used to prepare test pieces for measuring physical properties at a temperature of 250 ° C., and various physical properties were measured. The results are shown in Tables 2 to 4.

The amount of residual metal elements in each sample was quantified with an energy dispersive X-ray analyzer (Ultra Trace System manufactured by Rigaku Corporation) and an atomic absorption spectrometer. The results are shown in Tables 2 to 4.

[0052]

[Table 2]

[0053]

[Table 3]

[0054]

[Table 4]

The heat stabilizer (* 1) in Table 4 is octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate (IR manufactured by Ciba Geigy).
GANOX 1076) and a lubricant (* 2) are ethylene-bis-stearyl amide (trade name: EB- manufactured by Kao Corporation).
P) is shown.

Test methods for measuring physical properties (1) HDT (heat distortion temperature): under a load of 18.6 kg / cm ² ,
It was measured according to ASTM D-648. (2) Izod impact strength: Measured according to ASTM D-256 using a 1/4 inch thick notched test piece. (3) MFR: JIS temperature of 265 ° C, load of 10 kg, JIS
It was measured according to K-6874.

As is clear from the results shown in Tables 2 to 3, the compositions of Examples 1 to 10 all had a residual metal element content of 2000 ppm or less, and had excellent heat resistance, impact resistance and molding processability. Have sex.

On the other hand, as shown in Table 3, the compositions of Comparative Examples 1 and 2 are resin compositions containing no maleimide-type copolymer as the component (A), and therefore have heat resistance. Is low.

In Comparative Examples 3 to 8 in Table 4, the residual metal element content exceeds 2000 ppm, and therefore the balance of heat resistance, impact resistance and moldability is inferior to that of the Examples.

For example, in Examples 1 to 8, the HDT (heat distortion temperature) is around 110 ° C. and the impact strength is 20 kg · cm / c.
m or more and MFR is 50 g / 10 min or more. on the other hand,
Comparative Examples 3 to 7 have almost the same HDT level,
Izod impact strength is less than 10kgcm / cm and MFR
Is less than 35g / 10 minutes, and the balance is very bad.

Further, comparing Comparative Example 1 and Comparative Example 2,
Although the residual metal amount of Comparative Example 1 exceeds 2000 ppm and the residual metal amount of Comparative Example 2 is 2000 ppm or less, the balance between Izod impact strength and MFR is almost the same. From this fact and the previous example, the residual metal amount was 200% only when the maleimide copolymer was contained in the resin composition.
When the content is 0 ppm or less, the balance between heat resistance, impact resistance and moldability is remarkably improved.

[0062]

EFFECT OF THE INVENTION The thermoplastic resin composition of the present invention is a resin composition comprising a maleimide copolymer and a graft copolymer, and when the residual metal element content is 2000 ppm or less, heat resistance, impact resistance and It has excellent moldability. The thermoplastic resin composition of the present invention is required to have these performances, automobile parts, electric / electronic parts, office equipment parts, heat appliances, tableware, refrigerator parts, bath parts, shower parts, water purifier parts, toilet seats. And the like can be applied particularly effectively.

─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. ⁶ Identification code Internal reference number FI Technical display location C08L 33/18 LJK LJN 35/00 LJW 35/06 LJW 51/04 LKX LKY 55/02 LMB LME

Claims (3)

[Claims] 1. A component (A): an aromatic vinyl monomer residue,
5 to 50 parts by weight of maleimide-based copolymer consisting of unsaturated dicarboxylic acid imide derivative residue and vinyl monomer residue copolymerizable therewith, component (B): aromatic vinyl monomer residue, cyan 0 to 50 parts by weight of a vinyl aromatic-based copolymer comprising a vinyl chloride monomer residue and a vinyl monomer residue copolymerizable therewith, (C) component: a rubber-like polymer, aromatic vinyl A resin composition comprising 10 to 50 parts by weight of a graft copolymer obtained by graft polymerization of a monomer, a vinyl cyanide monomer, and a monomer mixture comprising a vinyl monomer copolymerizable therewith. The total amount of the components (A), (B) and (C) is 100 parts by weight], and the amount of residual metal elements in the resin composition is 2000 ppm or less. 2. The resin composition according to claim 1, wherein the component (A): aromatic vinyl monomer residue 40 to 80% by weight, unsaturated dicarboxylic acid imide derivative residue 10 to 60% by weight, and these 0-20% by weight of vinyl monomer residue copolymerizable with
5 to 50 parts by weight of a maleimide-based copolymer consisting of (B)
Components: 60 to 80% by weight of aromatic vinyl monomer residues, 20 to 40% by weight of vinyl cyanide monomer residues, and 0 to 20% by weight of vinyl monomer residues copolymerizable therewith. 0 to 50 parts by weight of vinyl aromatic copolymer, component (C):
35 to 65 parts by weight of a rubber-like polymer, 50 to 80% by weight of an aromatic vinyl monomer, 20 to 40% by weight of a vinyl cyanide monomer, and 0 to 30 of a vinyl monomer copolymerizable therewith.
The thermoplastic resin composition according to claim 1, which comprises 10 to 50 parts by weight of a graft copolymer obtained by graft-polymerizing 35 to 65 parts by weight of a monomer mixture consisting of 1% by weight. 3. The thermoplastic resin composition according to claim 1, wherein the residual metal element according to claim 1 is at least one metal composed of magnesium, calcium, or zinc.