JP2000119484A - Flame retardant resin composition - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide flame retardant styrenic resin compositions excellent in moldability and flame retardance and hard to undergo heat deterioration. SOLUTION: Flame retardant styrenic resin compositions comprise a mixture of 100 pts.wt. styrenic polymer having an islands-sea structure constituted by a polymer composed of at least a styrenic monomer and an unsaturated nitrile monomer as the sea-phase component (S) and 5-35 wt.% rubber-like polymer component grafted with these monomers and occluded with a copolymer of these monomers as the islands-phase component with a ratio of an AA chain component of a double-chain of the unsaturated nitrile monomer (A) in the sea-phase component (S) being not less than 15% and a reduced viscosity (ηsp/c) of (S) being 0.2-0.65 dl/g and 1-30 pts.wt. phosphate ester compound.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

TECHNICAL FIELD The present invention relates to a flame-retardant resin composition having excellent moldability and flame retardancy. For more information,
The present invention relates to a flame-retardant resin composition having excellent moldability and being resistant to thermal deterioration.

[0002]

2. Description of the Related Art Hitherto, styrene resins have been known as resins having excellent moldability and impact resistance, and have been used as molding materials. Therefore, the resin material to be used is selected according to the physical properties required for the molded article. For example, there are automobile parts, household electric parts, office equipment parts, mechanical parts, and the like, and in some cases, these resin materials are required to have flame retardancy. Resin materials generally used as alloys of styrenic polymers, especially ABS resins, include polycarbonate, vinyl chloride, and PBT. These materials exhibit self-extinguishing properties when burned, but they are alloyed with styrenic polymers. There is a disadvantage that flame retardancy is reduced.

In this case, when ABS and polycarbonate are alloyed, a flame retardant such as a halogen-based flame retardant or a phosphorus-based flame retardant is used to prevent a decrease in flame retardancy. (Japanese Patent Application No. 4-138080, EP174
However, a resin composition containing a halogen-based flame retardant may be thermally decomposed at the time of molding, and thus may have a problem in use. For this reason, phosphate ester-based flame retardants have been used. However, when ordinary ABS-based resins are used, phosphates have a low melting point and are in a liquid state, resulting in poor compounding processability. There is a problem that physical properties such as heat resistance are inferior.

In order to solve this problem, polytetrafluoroethylene, polysiloxane compounds, etc. are contained,
Methods for improving heat resistance and flammability have been proposed.
However, these additives are very expensive and may cause poor appearance due to poor dispersion.

[0005]

The styrene resin alone has good physical properties, especially when alloyed, has a small decrease in flame retardancy, significantly improves moldability, and has good heat resistance. Therefore, development of a method for providing a resin composition having further improved impact strength at low cost has been desired.

[0006]

The inventor of the present invention has conducted various studies to improve these drawbacks. As a result, pyrolysis gas chromatography of the sea-phase component (S) of the styrenic polymer (I) was carried out. Of the chain distribution of unsaturated nitrile monomer (A) in the sea phase component observed when measured in
The present inventors have found that the amount of the AA chain component affects the flammability and completed the present invention.

That is, the present invention provides a polymer comprising at least a styrene-based monomer and an unsaturated nitrile-based monomer, and if necessary, another monomer copolymerizable with the above-mentioned monomer. Further, an island phase component composed of a rubbery polymer component obtained by grafting at least one of these monomers and occluding a copolymer of the above monomer is further added to 5
Of the unsaturated nitrile monomer (A) in the sea phase component (S) contained in the sea phase component (S) as measured by pyrolysis gas chromatography of the sea phase component (S). A styrene polymer in which the AA chain component which is a double chain is observed at a rate of 15% or more, and the reduced viscosity (η _{sp / c} ) of the sea phase component (S) is 0.2 to 0.65 dl / g. (I) An object of the present invention is to provide a flame-retardant resin composition obtained by mixing 1 to 30 parts by weight of a phosphate compound with respect to 100 parts by weight.

The styrenic polymer (I) 10 described above
To 500 parts by weight and (II) 100 parts by weight of a resin component composed of 100 parts by weight of a thermoplastic polycarbonate, and 1 to 30 parts by weight of a phosphoric ester compound is mixed with the flame retardant resin composition. It is to be.

[0009]

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
In the present invention, the chain distribution of the unsaturated nitrile monomer component contained in the sea phase component (S) of the styrene polymer (I) is particularly important. Here, the sea-phase component (S) of the styrene-based polymer is a component obtained by removing the insoluble component of the mixture of methyl ethyl ketone and methanol 7: 3 (volume) from the styrene-based polymer, and is an unsaturated nitrile-based monomer. For the chain component of the components, the sea phase component (S) was subjected to a furnace-type pyrolysis gas chromatography to determine the molar concentration of each of the two chains among the decomposed components at 580 ° C., and the respective chain component ratios were obtained. Was.

In the present invention, it is necessary that the AA component which is a double chain in the chain distribution of the unsaturated nitrile monomer component (A) accounts for at least 15% of all the observed A components. is there. When the AA chain of the unsaturated nitrile monomer component in the sea phase component is less than 15% of the A component in which the AA chain is observed, the flame retardancy is reduced and the impact strength is reduced.
Not preferred.

The reduced viscosity range of the sea-phase component (S) excluding the insoluble component of the mixture of methyl ethyl ketone and methanol 7: 3 (volume) from the styrene polymer (I) used in the present invention is 0.2. 0.65 dl / g, preferably 0.25 to 0.55 dl / g, more preferably 0.3 to dl / g.
0.5 dl / g. If the reduced viscosity is less than 0.2 dl / g, the impact strength is remarkably reduced, which is not preferable. If the reduced viscosity is more than 0.65 dl / g, the fluidity is lowered, and the impact resistance is lowered.

Here, the reduced viscosity means that 0.25 g of the sea-phase component (S) is precisely weighed and dissolved in 50 ml of dimethylformamide for 2 hours.
The value obtained by measuring at 30 ° C environment using an Ubbelohde viscometer of 100 seconds, a reduced viscosity is obtained falling seconds of the solvent (t ₀₎ and a solution of falling seconds (t) by the following equation .

Reduced viscosity (η _{SP / C} ) = {(t / t ₀ ) −1} /0.5

The styrenic polymer of the present invention has a content of the first or second group metal of the periodic table of 100 wt.% Produced by emulsion polymerization, solution polymerization or bulk polymerization. pp
m or less are used. Preferably solution polymerization or
It is manufactured by the bulk polymerization method.

The styrenic polymer (I) of the present invention needs to contain 5 to 35 parts by weight of a rubbery component obtained by grafting and occluding a monomer and a copolymer of the monomer, that is, an island phase component. is there. If the content of the island phase component is 5 parts by weight or less, the impact strength is not sufficient, and if the content is 35 parts by weight or more, the moldability is deteriorated and the heat resistance is poor.

In the present invention, it is particularly preferably used as a mixture of the thermoplastic polycarbonate (II) and the ABS polymer (I). The mixing ratio of (I) is 10 to 500 parts by weight, preferably 30 to 400 parts by weight, more preferably 50 to 30 parts by weight, based on 100 parts by weight of (II).
0 parts by weight.

If (I) is less than 10 parts by weight per 100 parts by weight of (II), the thickness dependency of impact strength is increased, and if it is more than 500 parts by weight, the inherent properties of polycarbonate are impaired. .

Further, in addition to (I) or (I) and (II), a mixture of other ABS-based polymer or other polymer or an additive, if necessary, is also included in the constitution of the present invention. . For example, as other polymer, styrene-acrylonitrile resin, butadiene rubber, SBR, ethylene-propylene rubber, acrylic elastomer such as acrylate-butadiene copolymer and the like are preferable. In this case, the addition amount of the other polymer is 0 to 20% by weight based on (I) or (I) and (II), and the flame retardancy is good if it is 20% by weight or less.

The styrenic polymer referred to in the present invention means an aromatic vinyl monomer, an unsaturated nitrile monomer and, if necessary, a vinyl monomer copolymerizable therewith in the presence of a conjugated diene polymer. A graft copolymer resin obtained by polymerizing a monomer mixture composed of a monomer. Examples of the conjugated diene-based polymer constituting the graft copolymer resin include polybutadiene, butadiene-styrene copolymer, butadiene-acrylonitrile copolymer, polyisoprene, and polychloroprene. This conjugated diene polymer is a kind,
Alternatively, a mixture of two or more kinds may be used.

Styrene α is used as the aromatic vinyl monomer.
-Methylstyrene, dimethylstyrene, vinyltoluene and the like.

Examples of the unsaturated nitrile monomer include acrylonitrile, methacrylonitrile and the like. In the present invention, when the content of the unsaturated nitrile monomer is small, the AA double chain is reduced, so that 15 to 40% by weight is used in the resin.

The vinyl monomers copolymerizable therewith include methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate, hydroxyethyl acrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, maleimide, N -Phenylmaleimide and the like. These monomers may be one kind or a mixture of two or more kinds.

Among the methods for producing an ABS polymer in the present invention, a solution polymerization or a bulk polymerization method is particularly preferred, and a specific production method is an unsaturated polymer used in the polymerization to make the AA chain component 15% or more. Until 50% by weight of the nitrile monomer component is polymerized, the ratio of the unsaturated nitrile monomer component to the other monomer in the polymerization solution is always 2%.
It is necessary to carry out polymerization while keeping the content at 5 mol% or more.

For example, a rubbery polymer synthesized by solution polymerization is dissolved in a monomer containing the above-mentioned monomer component and, if necessary, in a solvent such as ethylbenzenetoluene or methylethylketone, and a molecular weight regulator and a polymerization initiator are dissolved. With or without addition, a monomer solution of the rubber-like polymer is continuously supplied to a stirred reactor, and a part or all of the monomer is copolymerized to prepare a rubber-like polymer component. Form particles. At this time, the rubbery polymer component is 0.1 μm to 3 μm.
m so as to form a dispersed phase as particles. This is achieved by controlling the amount of the rubber-like polymer, the amount of the molecular weight regulator, the amount of the polymerization initiator used, the polymerization temperature and the stirring speed to control the particles of the rubber-like polymer component to 0.1 μm to 3 μm, The polymer mixture obtained after adjusting the conversion so as to contain the polymer component in an amount of 5 to 35 parts by weight is introduced into a devolatilization tank, and the solvent is used when the unreacted monomer and the solvent are contained. Separates from polymer components. Thereafter, through a granulation step, a resin component (I) in a pellet form is obtained.

In the present invention, when used together with the styrene polymer (I), the polycarbonate (II) may be an aromatic polycarbonate, an aliphatic polycarbonate or an aliphatic polycarbonate.
Aromatic polycarbonate and the like can be mentioned.

Generally, the polycarbonate is prepared by a solvent method,
That is, a known acid acceptor in a solvent such as methylene chloride,
The so-called phosgene method of reacting a dihydric phenol with a carbonate precursor such as phosgene in the presence of a molecular weight regulator,
A typical example is an aromatic polycarbonate resin obtained by a transesterification method in which a dihydric phenol is reacted with a carbonate precursor such as diphenyl carbonate. Suitable dihydric phenols include bisphenols, and 2,2-bis (4-hydroxyphenyl) propane (bisphenol A) is particularly preferred. Further, depending on the purpose, a polymer obtained by substituting part or all of bisphenol A with another dihydric phenol or a polymer using bisphenols substituted with halogen may be used. The aromatic polycarbonate resin has a viscosity average molecular weight of 10,000 from the viewpoint of mechanical strength and moldability.
It is preferably from 0 to 100,000, and in particular,
The thing of 00-40,000 is suitable.

The flame retardant used in the present invention is a phosphoric ester compound, and various types can be used without any particular limitation. Specific examples of the phosphoric acid ester-based compound include trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, tributoxyethyl phosphate, triphenyl phosphate, tricresyl phosphate, cresyl phenyl phosphate, octyl diphenyl phosphate, and diisopropyl phenyl phosphate. , Tris (chloroethyl) phosphate, tris (dichloropropyl) phosphate, tris (chloropropyl) phosphate, bis (2,3-dibromopropyl) -2,3-dichloropropylphosphate, tris (2,3-dibromopropyl) phosphate and Bis (chloropropyl)
Monooctyl phosphate, bisphenol A tetraphenyl diphosphate, bisphenol A tetracresyl diphosphate, bisphenol A tetraxylyl diphosphate, hydroquinone tetraphenyl diphosphate, hydroquinone tetracresyl diphosphate, hydroquinone tetraxylyl diphosphate, and the like are preferred. Triphenyl phosphate and various bisphosphates.

The above-mentioned component is the component (I) or (I)
And 1 to 30 parts by weight, preferably 3 to 20 parts by weight, more preferably 5 to 1 part by weight based on 100 parts by weight of the total of (II) and (II).
Add 5 parts by weight. If the amount of the component is less than the above range, the effect of the present invention is not sufficiently exhibited, and if it is more than the above range, heat resistance is impaired.

The flame-retardant resin composition according to the present invention may contain, in addition to the above-mentioned components, other components commonly used in mixing resins, molding, etc., depending on the purpose, as long as the physical properties are not impaired. Additives such as pigments, dyes, reinforcing materials (glass fiber,
Well-known additives such as carbon fibers, fillers (carbon black, silica, titanium oxide, etc.), antioxidants, weathering agents, lubricants, release agents, plasticizers, antistatic agents and the like can be blended.

The method for producing the resin composition of the present invention is not particularly limited, and a known method can be used, but a melt mixing method is generally preferred. Examples of the device include an extruder, a Banbury mixer, a roller, a kneader, and the like. These devices can be operated batchwise or continuously. The order of mixing the components is not particularly limited.

[0031]

The present invention will be described in more detail with reference to the following examples. The present invention is not limited to the following examples unless it exceeds the gist. The “part” and “%” ratios are based on weight.

In each of the following Examples and Comparative Examples, the physical properties of the flame-retardant resin composition were measured by the following methods. 1. Flexural modulus (MPa) A molded product is cut out into a test piece, and a bending test method (JIS K
7203). 2. Izod impact strength (with notch) (KJ / m ² ) A molded product was cut into a test piece and measured according to the Izod impact test method (JIS K7110). 3. Measurement of heat resistance temperature (ΔC) The Vicat softening point was measured using a sample obtained by cutting a test piece from a molded product in accordance with JIS K7206. 4. Flammability Based on subject 94 (UL94) standardized by Underwriters Laboratories (UL)
A 1.6 mm thick combustion test was performed and V-0, V-1,
It was classified and displayed in the flame retardant class of V-2. In a burning test, it was also determined whether or not a flaming drop would ignite dry surgical cotton wool 12 inches (305 mm) below the sample. 5. Observation of mold adhering substance Cylinder temperature of molding machine 260 ° C, mold temperature 60 °
C, adhering matter inside the gas vent of the mold after 250 shots was visually observed.
Was determined.

[0033]

Example 1 (II) Thermoplastic polycarbonate A commercially available polycarbonate polymer was used. The following table shows the features.

[0034]

[Table 1] *: Measurement conditions: 230 ° C, 10 kg

(I) Production of ABS polymer 60 parts by weight of styrene, 20 parts by weight of acrylonitrile, 15 parts by weight of ethylbenzene, 10 parts by weight of butadiene copolymer, 0.05 parts by weight of organic peroxide, tertiary decyl mercaptan 0 A raw material solution consisting of 0.08 parts by weight was prepared, and the raw material was continuously supplied to a four-stage stirred polymerization tank row reactor to perform polymerization. Average reaction temperature of the first tank 1
The temperature was set to 105 ° C. in the second tank, and to 120 ° C. in the third tank, and 125 ° C. in the fourth tank. From the fourth tank, the polymerization liquid was led to a separation and recovery step comprising a preheater and a decompression chamber.

The resin discharged from the recovery step was subjected to an extrusion step to obtain an ABS-based polymer (styrene-based polymer (I)) as granular pellets. The reduced viscosity of the polymer component (P) of the obtained ABS polymer was 0.45 dl / g, the acrylonitrile content was 25%, the graft ratio was 62%, and the rubbery polymer content was 19.2%. Was. The particle size of the rubbery polymer component was 1.1 μm. The chain component of the unsaturated nitrile monomer component, which is a component obtained by removing the insoluble component of the mixture of methyl ethyl ketone and methanol 7: 3 (volume) from the polymer (P), is a sea phase component (S) in a heating furnace type. Using pyrolysis gas chromatography, of the components decomposed at 580 ° C,
The molar concentration of each trimer component was determined, and the ratio of each chain component was determined. AA, which is a double chain in the chain distribution of the acrylonitrile monomer component (A), was obtained.
The chain component was 17.9% of the observed A component.
(ABS-1) [Polycarbonate / ABS flame-retardant resin composition] 100 parts by weight of the polycarbonate of the above (II) and the above (I)
Extruder, 100 parts by weight of the ABS polymer obtained in the above, 10 parts by weight of a phosphate ester-based flame retardant (aromatic phosphate-based oligomer: CR-733S, Daihachi Chemical Co., Ltd.), and 0.2 part by weight of an antioxidant. At 220 ° C. Table 2 shows the results of preparing and evaluating test pieces from the obtained pellets. Before the extrusion operation, both the ABS polymer and the polycarbonate were dried at 100 ° C. for 12 hours.

Example 2 Table 2 shows the evaluation results of only the ABS polymer obtained in Example 1.
Shown in

Example 3 From 46 parts by weight of styrene, 23 parts by weight of acrylonitrile, 15 parts by weight of ethylbenzene, 12 parts by weight of a styrene-butadiene block copolymer, 0.05 part by weight of an organic peroxide, and 0.15 part by weight of tertiary decyl mercaptan. A raw material solution was prepared and polymerized in the same manner as in Example 1.

The reduced viscosity of the polymer component (P) of the obtained ABS polymer was 0.37 dl / g, the acrylonitrile compound content was 28%, the graft ratio was 98%, and the particle size of the rubbery polymer component was 1.3 μm, the content of which is 2
5%. In addition, the ratio of each chain distribution was determined by measuring pyrolysis chromatography of the components excluding the insoluble components of the mixed solution of methyl ethyl ketone and methanol 7: 3 (volume) from the polymer (P). The acrylonitrile monomer component The AA chain component, which is a double chain in the chain distribution of (A), was 15.8% of the observed A component. (A
BS-2) The mixing of the polycarbonate, the ABS polymer and the flame retardant was the same as in Example 1. Table 2 shows the results.

Example 4 56 parts by weight of styrene, 20 parts by weight of acrylonitrile, 14 parts by weight of ethylbenzene 10 parts by weight of a rubbery polymer (used in Example 1), organic peroxide (used in Example 1) Example 1 was the same as Example 1 except that 0.05 part by weight and 0.18 part by weight of tertiary decyl mercaptan were used. The reduced viscosity of the polymer component (A) of the obtained ABS polymer was 0.4 dl / g, and the acrylonitrile content was 24.
%, The graft ratio was 72%, the particle size of the rubbery polymer component was 0.8 μm, and the content was 22.0%.
Further, the ratio of each chain distribution was determined by measuring pyrolysis gas chromatography of the components excluding the insoluble components of the mixed solution of methyl ethyl ketone and methanol 7: 3 (volume) from the polymer (P). As a result, the acrylonitrile monomer was obtained. In the chain distribution of the component (A), the AA chain component, which is a double chain, was 17.1% of the observed A component. (ABS-
3) Table 2 shows the results obtained by mixing 67 parts by weight of the obtained styrene-based polymer and a flame retardant in the same manner as in Example 1 with respect to 100 parts by weight of polycarbonate.

Example 5 62 parts by weight of styrene, 23 parts by weight of acrylonitrile, 15 parts by weight of ethylbenzene 9 parts by weight of a rubbery polymer (used in Example 1), and organic peroxide (used in Example 1) 0.045 parts by weight, 0.26 parts by weight of tertiary decyl mercaptan, average reaction temperature of the first stage tank 97 °
C, 100 ° C in the second tank, 120 ° C in the third tank
The ABS polymer was obtained at 130 ° C in the fourth tank at ° C. The reduced viscosity of the polymer component (A) of the obtained ABS polymer was 0.35 dl / g. The acrylonitrile content was 25%, the graft ratio was 120%, the particle size of the rubbery polymer component was 2.2 μm, and the content was 19.8.
%Met. The chain distribution ratio of each component was determined by measuring pyrolysis gas chromatography of the components excluding the insoluble component of the mixture of methyl ethyl ketone and methanol 7: 3 (volume) from the polymer (P), and the acrylonitrile monomer component was determined. In the chain distribution of (A), the AA chain component, which is a double chain, was 17.5% of the observed A component. (A
BS-4) The results obtained by mixing 300 parts by weight of the obtained styrenic polymer and 100 parts by weight of the polycarbonate and the flame retardant in the same manner as in Example 1 are shown in Table 2.

Example 6 The procedure of Example 1 was repeated except that 100 parts by weight of the polycarbonate of Example 1 and 20 parts by weight of the phosphoric ester flame retardant used in Example 1 were mixed. Table 2 shows the results.

Comparative Example 1 60 parts by weight of styrene, 20 parts by weight of acrylonitrile, 15 parts by weight of ethylbenzene 10 parts by weight of a rubbery polymer (used in Example 1), and organic peroxide (used in Example 1) 0.05 parts by weight, 0.18 parts by weight of tertiary decyl mercaptan, reaction temperature of the first stage tank 105 °
C, 120 ° C in the second tank, 130 in the third tank
The procedure was the same as in Example 1 except that the temperature was set to ° C. AB obtained
The reduced viscosity of the polymer component (A) of the S-based polymer is 0.68 d.
1 / g, the acrylonitrile compound content was 23%, the graft ratio was 70%, the particle size of the rubbery polymer component was 1.0 μm, and the content was 18 parts by weight. From the polymer (P), methyl ethyl ketone and methanol 7: 3
(Amount) of the mixture excluding the insoluble component was measured by pyrolysis gas chromatography to determine the respective chain distribution ratios. As a result, AA which is a double chain in the chain distribution of the acrylonitrile monomer component (A) was obtained. A where a chain component is observed
17.5% of the components. (ABS-5) Table 3 shows the results obtained by mixing 300 parts by weight of the styrenic polymer obtained and 100 parts by weight of the polycarbonate with a flame retardant in the same manner as in Example 1.

Comparative Example 2 From 62 parts by weight of styrene, 15 parts by weight of acrylonitrile, 20 parts by weight of ethylbenzene, 12 parts by weight of a styrene-butadiene block copolymer, 0.05 part by weight of an organic peroxide, and 0.20 part by weight of tertiary decyl mercaptan. A raw material solution was prepared and polymerized in the same manner as in Example 1.

The reduced viscosity of the polymer component (P) of the obtained ABS polymer was 0.37 dl / g, the acrylonitrile content was 16%, the graft ratio was 98%, and the particle size of the rubbery polymer component was 1 0.3 μm, and its content was 25%. Further, the ratio of each chain distribution was determined by measuring pyrolysis gas chromatography of the components excluding the insoluble components of the mixed solution of methyl ethyl ketone and methanol 7: 3 (volume) from the polymer (P). As a result, the acrylonitrile monomer was obtained. In the chain distribution of the component (A), the AA chain component, which is a double chain, was 12.8% of the observed A component. Also,
The first or second group metal of the periodic table contains 100 wt. ppm or less. (ABS-6). Polycarbonate and AB
The mixing of the S polymer and the flame retardant was the same as in Example 1. Table 3 shows the results.

Comparative Example 3 The procedure of Example 1 was repeated except that 100 parts by weight of the polycarbonate of Example 1 and 35 parts by weight of the phosphoric ester flame retardant used in Example 1 were mixed. Table 3 shows the results.

[0047]

[Table 2]

[0048]

[Table 3]

[0049]

According to the present invention, a styrene resin composition or a polycarbonate / styrene resin composition excellent in flame retardancy, heat resistance and impact strength can be provided, which is very industrially significant.

Continued on the front page (72) Inventor Ryuichi Sugimoto 1-6-6 Takasago, Takaishi City, Osaka Prefecture Mitsui Chemicals, Inc. (72) Inventor Masato 1-6 Takasago, Takaishi City, Osaka Mitsui Chemicals, Inc. 4J002 BC06W BC061 BG10W BG101 BN142 BN152 CG01X CG013 EW046 EW056 FA040 FD010 FD136

Claims (3)

[Claims] 1. A polymer comprising at least a styrene-based monomer and an unsaturated nitrile-based monomer, and if necessary, another monomer copolymerizable with the monomer, as a sea-phase component, and at least a sea-phase component. 5 to 35 parts by weight of an island phase component consisting of a rubbery polymer component obtained by grafting these monomers and occluding a copolymer of the above monomers, and a sea phase component (S)
In the sequence distribution of unsaturated nitrile monomer (A) in the sea phase component (S) observed when measured by pyrolysis gas chromatography of AA, a double-chain AA chain component is 15% or more. And a phosphoric ester based on 100 parts by weight of a styrene polymer (I) having a reduced viscosity (η _{sp / c} ) of 0.2 to 0.65 dl / g of the sea phase component (S). A flame-retardant resin composition obtained by mixing 1 to 30 parts by weight of a compound. 2. The styrene-based polymer (I) is the first compound of the periodic table.
2. The flame-retardant resin composition according to claim 1, wherein the composition contains no more than 100 ppm of a Group 2 metal. 3. A phosphoric acid ester compound (1) to a resin component comprising 10 to 500 parts by weight of the styrenic polymer (I) according to claim 1 and 100 parts by weight of a thermoplastic polycarbonate (II). A flame-retardant resin composition mixed at a ratio of 30 parts by weight.