JP5378712B2 - Flame retardant resin composition and molded product therefrom - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a flame-retardant resin composition using vegetable-origin raw materials, which has high flame retardancy and good physical properties, and a molded article therefrom. <P>SOLUTION: The flame-retardant resin composition contains (B) 1-100 pts.wt. of an organophosphorus compound (component B) represented by formula (1) based on (A) 100 pts.wt. of a resin component (component A) containing at least 50 wt.% of a polycarbonate resin containing a polycarbonate constituent unit represented by formula (A-1), wherein X<SP>1</SP>and X<SP>2</SP>are identical or different aromatic substituted alkyl groups. <P>COPYRIGHT: (C)2010,JPO&amp;INPIT

Description

  The present invention relates to a flame retardant resin composition using a plant-derived raw material having high flame retardancy and good physical properties, and a molded article therefrom. More particularly, the present invention relates to a flame retardant resin composition containing a specific organophosphorus compound and substantially free of halogen, and a molded article therefrom.

  Generally, polypropylene (PP), acrylonitrile-butadiene-styrene (ABS), polyamide (PA6, PA66), polyester (PET, PBT), polycarbonate (PC), etc. are used as raw materials for resin molded products. Is used. However, these resins are manufactured using raw materials obtained from petroleum resources. In recent years, there are concerns about problems such as depletion of petroleum resources and the global environment, and raw materials obtained from biological materials such as plants are used. There is a demand for the production of resin. Considering the problem of the global environment in particular, the resin that uses plant-derived materials is considered to be carbon neutral because it is neutral as a carbon balance, considering the amount of carbon dioxide absorbed during plant growth even if incinerated after use. It is considered to be a resin with a low impact on the global environment.

  On the other hand, when resins using these plant-derived raw materials are used for industrial materials, particularly electrical / electronic parts, OA-related parts, or automobile parts, it is necessary to impart flame retardancy for safety reasons.

  Until now, various attempts have been made for flame retarding of resins using plant-derived materials, particularly polylactic acid resins, and a certain degree of flame retarding has been achieved. However, these flame retardant formulations use a large amount of flame retardant, and impair the original physical properties of the resin.

  On the other hand, as a resin using a plant-derived raw material, a polycarbonate resin using a raw material obtained from an ether diol residue that can be produced from a saccharide, in addition to a polylactic acid resin, has been studied.

に示したエーテルジオールは、たとえば糖類およびでんぷんなどから容易に作られ、３種の立体異性体が知られているが、具体的には下記式（ｂ）に示す、１，４：３，６−ジアンヒドロ−Ｄ−ソルビトール（本明細書では以下「イソソルビド」と呼称する）、

下記式（ｃ）に示す、１，４：３，６−ジアンヒドロ−Ｄ−マンニトール（本明細書では以下「イソマンニド」と呼称する）、

下記式（ｄ）に示す、１，４：３，６−ジアンヒドロ−Ｌ−イジトール（本明細書では以下「イソイディッド」と呼称する）である。

For example, the following formula (a)

The ether diol shown in Fig. 1 is easily made from sugars and starch, for example, and three stereoisomers are known. Specifically, 1,4: 3,6 shown in the following formula (b) -Dianhydro-D-sorbitol (hereinafter referred to as "isosorbide"),

1,4: 3,6-dianhydro-D-mannitol (hereinafter referred to as “isomannide”) shown in the following formula (c),

1,4: 3,6-dianhydro-L-iditol (hereinafter referred to as “isoidid” in the present specification) represented by the following formula (d).

  Isosorbide, isomannide, and isoidide are obtained from D-glucose, D-mannose, and L-idose, respectively. For example, isosorbide can be obtained by hydrogenating D-glucose and then dehydrating it using an acid catalyst.

  So far, among the above-mentioned ether diols, in particular, incorporation into polycarbonate using isosorbide as a monomer has been studied. Among them, isosorbide homopolycarbonate is described in Patent Documents 1 and 2.

Of these, Patent Document 1 reports a homopolycarbonate resin having a melting point of 203 ° C. using a melt transesterification method. However, this polymer has insufficient mechanical properties. As an example of high heat resistance, Patent Document 2 reports a polycarbonate having a glass transition temperature of 170 ° C. or higher as measured by differential calorimetry at a heating rate of 10 ° C./min. In some cases, the melt viscosity is too high. On the other hand, Patent Document 3 describes a copolymerized polycarbonate of isosorbide and a linear aliphatic diol.
Regarding these polycarbonates composed of isosorbide, none of these documents describes any flame retardancy.

British Patent Application No. 1079686 International Publication No. 2007/013463 Pamphlet International Publication No. 2004/111106 Pamphlet

The first object of the present invention is to provide a flame retardant resin composition using a plant-derived raw material having high flame retardancy and good physical properties, and a molded product therefrom.
A second object of the present invention is to provide a flame retardant resin composition containing a specific organophosphorus compound and substantially halogen-free, and a molded article therefrom.

According to the study by the present inventors, the object of the present invention is as follows.
(A) With respect to 100 parts by weight of a resin component (component A) containing at least 50% by weight of a polycarbonate resin (component A-1) containing a carbonate constituent unit represented by the following formula (A-1), (B) This is achieved by a flame retardant resin composition containing 1 to 100 parts by weight of an organophosphorus compound (component B) represented by the following formula (1) and a molded product therefrom.

（式中、Ｘ^１、Ｘ^２は同一もしくは異なり、下記式（２）で表される芳香族置換アルキル基である。）

(In formula, X < ¹ >, X < ² > is the same or different, and is an aromatic substituted alkyl group represented by following formula (2).)

（式中、ＡＬは炭素数１〜５の分岐状または直鎖状の脂肪族炭化水素基であり、Ａｒは置換基を有しても良いフェニル基、ナフチル基、またはアントリル基である。ｎは１〜３の整数を示し、ＡｒはＡＬ中の任意の炭素原子に結合することができる。）

(In the formula, AL is a branched or linear aliphatic hydrocarbon group having 1 to 5 carbon atoms, and Ar is a phenyl group, a naphthyl group, or an anthryl group which may have a substituent. Represents an integer of 1 to 3, and Ar can be bonded to any carbon atom in AL.)

According to this invention, the flame-retardant resin composition using the plant-derived raw material which achieves high flame retardance without impairing the original characteristic of resin is obtained.
Hereinafter, the flame retardant resin composition of the present invention will be described in more detail.

  In the present invention, the polycarbonate resin (component A-1) is a polycarbonate resin containing a carbonate structural unit represented by the following formula (A-1), and is represented by the following formula (A-1) in all carbonate structural units. The structural unit is preferably 50 mol% or more, more preferably 60 mol% or more, further preferably 70 mol% or more, particularly preferably 80 mol% or more, and most preferably 90 mol% or more.

  Further, in the present invention, the resin component is sufficient if the polycarbonate resin (component A-1) occupies the main component in the constituent resin component (component A), and the polycarbonate resin (component A-1) is at least 50% by weight, preferably May be at least 60% by weight, more preferably at least 70% by weight, even more preferably at least 80% by weight, particularly preferably at least 90% by weight. The other resin (component A-2) is 50% by weight or less, preferably 40% by weight or less, more preferably 30% by weight or less, further preferably 20% by weight or less, particularly preferably 10% by weight or less in the component A. May be. Other resins will be described in detail later.

  The polycarbonate resin (A-1 component) in the constituent resin component (A component) of the present invention has a biogenic substance content of 25% or more, preferably 50% or more, particularly preferably measured according to ASTM D686605. Is 70% or more. Due to the nature of the present invention, it is better that the content of the biogenic substance is high.

In the polycarbonate resin (component A-1), the lower limit of the specific viscosity at 20 ° C. of a solution obtained by dissolving 0.7 g of resin in 100 ml of methylene chloride is preferably 0.14 or more, more preferably 0.20 or more. Preferably it is 0.22 or more. The upper limit is preferably 0.45 or less, more preferably 0.37 or less, and still more preferably 0.34 or less. When the specific viscosity is lower than 0.14, it becomes difficult to give sufficient mechanical strength to the molded product obtained from the polycarbonate resin composition of the present invention. On the other hand, when the specific viscosity is higher than 0.45, the melt fluidity becomes too high, and the melting temperature having the fluidity necessary for molding becomes higher than the decomposition temperature. The polycarbonate resin (component A-1) has a melt viscosity of 0.08 × 10 ^{3 to} 2.4 × 10 ³ Pa · s measured with a capillary rheometer at 250 ° C. under a shear rate of 600 sec ^−1. Is preferably in the range of 0.1 × 10 ^{3 to} 2.0 × 10 ³ Pa · s, more preferably in the range of 0.1 × 10 ^{3 to} 1.5 × 10 ³ Pa · s. A range is further preferred. When the melt viscosity is within this range, the mechanical strength is excellent, and when molding using the polycarbonate resin composition of the present invention, silver is not generated during molding, which is good.

  The lower limit of the glass transition temperature (Tg) of the polycarbonate resin (A-1 component) used in the present invention is preferably 100 ° C. or higher, more preferably 120 ° C. or higher, and the upper limit is preferably 165 ° C. or lower. When Tg is less than 100 ° C., the heat resistance (particularly heat resistance due to moisture absorption) is poor, and when it exceeds 165 ° C., the melt fluidity at the time of molding using the polycarbonate resin composition of the present invention is poor. Tg is measured by DSC (model DSC2910) manufactured by TA Instruments.

  The lower limit of the 5% weight reduction temperature of the polycarbonate resin (component A-1) used in the present invention is preferably 300 ° C or higher, more preferably 320 ° C or higher, and the upper limit is preferably 400 ° C or lower. Preferably it is 390 degrees C or less, More preferably, it is 380 degrees C or less. It is preferable that the 5% weight loss temperature is in the above range since there is almost no decomposition of the resin when molding using the polycarbonate resin composition of the present invention. The 5% weight loss temperature is measured by TA Instruments TGA (model TGA2950).

で表されるエーテルジオールおよび炭酸ジエステルとから溶融重合法により製造することができる。エーテルジオールとしては、具体的には下記式（ｂ）、（ｃ）および（ｄ）で表されるイソソルビド、イソマンニド、イソイディッドなどが挙げられる。 The polycarbonate resin (A-1 component) used in the present invention has the following formula (a):

It can manufacture with the melt polymerization method from the ether diol and carbonic acid diester represented by these. Specific examples of the ether diol include isosorbide, isomannide, and isoidide represented by the following formulas (b), (c), and (d).

  These saccharide-derived ether diols are substances obtained from natural biomass and are one of so-called renewable resources. Isosorbide is obtained by hydrogenating D-glucose obtained from starch and then dehydrating it. Other ether diols can be obtained by the same reaction except for the starting materials.

  In particular, a polycarbonate resin in which the carbonate structural unit includes a carbonate structural unit derived from isosorbide (1,4: 3,6-dianhydro-D-sorbitol) is preferable. Isosorbide is an ether diol that can be easily made from starch, etc., and can be obtained in abundant resources. In addition, it is superior in terms of ease of manufacture, properties, and versatility compared to isomannide and isoidide. .

  Moreover, the polycarbonate resin (A-1 component) used for this invention is good also as copolymerization with aliphatic diols or aromatic bisphenol in the range which does not impair the characteristic. As the aliphatic diol, a linear aliphatic diol having 3 to 12 carbon atoms and an alicyclic diol having 6 to 20 carbon atoms are preferably used. Specific examples include linear diols such as 1,3-propanediol, 1,4-butanediol, and 1,6-hexanediol, and alicyclic alkylenes such as cyclohexanediol and cyclohexanedimethanol. Of these, 1,3-propanediol, 1,4-butanediol, 1,6-hexanediol, and cyclohexanedimethanol are preferred. In addition, since the present invention has as a main component the above-mentioned formula (a) obtained from renewable resources such as plants, plant-derived diols are also preferably used. Specific examples include diols containing a terpene component.

  As aromatic bisphenols, 2,2-bis (4-hydroxyphenyl) propane (commonly known as “bisphenol A”), 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) -3,3,5-trimethylcyclohexane, 4,4 '-(m-phenylenediisopropylidene) diphenol, 9,9-bis (4-hydroxy-3-methylphenyl) fluorene, 2,2-bis (4 -Hydroxy-3-methylphenyl) propane, 2,2-bis (4-hydroxyphenyl) -4-methylpentane, 1,1-bis (4-hydroxyphenyl) decane, 1,3-bis {2- (4 -Hydroxyphenyl) propyl} benzene and the like. These aliphatic diols and aromatic bisphenols can be used alone or in combination.

  Moreover, the polycarbonate resin (A-1 component) used for this invention can also introduce | transduce an end group in the range which does not impair the characteristic. Such end groups can be introduced by adding the corresponding hydroxy compound during polymerization. The terminal group is preferably a terminal group represented by the following formula (i) or (ii).

In the above formulas (i) and (ii), R ⁴ represents an alkyl group having 4 to 30 carbon atoms, an aralkyl group having 7 to 30 carbon atoms, a perfluoroalkyl group having 4 to 30 carbon atoms, or the following formula ( iii), preferably an alkyl group having 4 to 20 carbon atoms, a perfluoroalkyl group having 4 to 20 carbon atoms, or the following formula (iii), particularly an alkyl group having 8 to 20 carbon atoms, or The following formula (iii) is preferable. Y is preferably at least one bond selected from the group consisting of a single bond, ether bond, thioether bond, ester bond, amino bond and amide bond, more preferably selected from the group consisting of a single bond, ether bond and ester bond. It is at least one kind of bond, and among them, a single bond and an ester bond are preferable. a is an integer of 1 to 5, preferably an integer of 1 to 3, and 1 is particularly preferable.

In the formula (iii), R ⁵ , R ⁶ , R ⁷ , R ⁸ and R ⁹ are each independently an alkyl group having 1 to 10 carbon atoms, a cycloalkyl group having 6 to 20 carbon atoms, It is at least one group selected from the group consisting of an alkenyl group having 2 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms, and an aralkyl group having 7 to 20 carbon atoms, preferably each independently a carbon atom. And at least one group selected from the group consisting of an alkyl group having 1 to 10 carbon atoms and an aryl group having 6 to 10 carbon atoms, particularly at least one group independently selected from the group consisting of a methyl group and a phenyl group. Is preferred. b is an integer of 0 to 3, an integer of 1 to 3 is preferable, and an integer of 2 to 3 is particularly preferable. c is an integer of 4 to 100, preferably an integer of 4 to 50, and particularly preferably an integer of 8 to 50.

  Since the polycarbonate resin (component A-1) used in the present invention has a carbonate structural unit in the main chain structure using raw materials obtained from renewable resources such as plants, these hydroxy compounds are also recyclable from plants and the like. A raw material obtained from a resource is preferred. Examples of hydroxy compounds obtained from plants include long-chain alkyl alcohols having 14 or more carbon atoms (cetanol, stearyl alcohol, behenyl alcohol) obtained from vegetable oils.

  Moreover, the polycarbonate resin (A-1 component) used for this invention mixes the bishydroxy compound containing the ether diol represented by the said Formula (a), and carbonic acid diester, The alcohol or phenol produced | generated by a transesterification reaction is mixed. It can be obtained by performing melt polymerization by distillation under high temperature and reduced pressure.

  The reaction temperature is preferably as low as possible in order to suppress decomposition of the ether diol and obtain a highly viscous resin with little coloration, but the polymerization temperature is 180 ° C. to 280 ° C. in order to proceed the polymerization reaction appropriately. It is preferably in the range of ° C, more preferably in the range of 180 ° C to 270 ° C.

In the initial stage of the reaction, ether diol and carbonic acid diester are heated at normal pressure and pre-reacted, and then gradually reduced in pressure, and the system is changed to 1.3 × 10 ^{−3 to} 1.3 × 10 ^{− in the} late stage of the reaction. A method of facilitating the distillation of alcohol or phenol produced by reducing the pressure to about ⁵ MPa is preferred. The reaction time is usually about 1 to 4 hours.

  A polymerization catalyst can be used to increase the polymerization rate. Examples of the polymerization catalyst include sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogencarbonate, alkali metal compounds such as sodium salt or potassium salt of dihydric phenol, calcium hydroxide, barium hydroxide, magnesium hydroxide. And alkaline earth metal compounds such as tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrabutylammonium hydroxide, nitrogen-containing basic compounds such as trimethylamine and triethylamine. These may be used alone or in combination of two or more. Among these, it is preferable to use a nitrogen-containing basic compound and an alkali metal compound in combination.

The amount of these polymerization catalysts used is preferably in the range of 1 × 10 ⁻⁹ to 1 × 10 ⁻³ equivalents, more preferably 1 × 10 ^{−8 to} 5 × 10 ⁻⁴ equivalents, relative to 1 mol of the carbonic acid diester component. Chosen by The reaction system is preferably maintained in an atmosphere of a gas inert to the raw materials such as nitrogen, the reaction mixture, and the reaction product. Examples of inert gases other than nitrogen include argon. Furthermore, you may add additives, such as antioxidant, as needed.

  The carbonic acid diester used for the production of the polycarbonate resin (component A-1) used in the present invention is an optionally substituted ester such as an aryl group having 6 to 20 carbon atoms, an aralkyl group or an alkyl group having 1 to 18 carbon atoms. Is mentioned. Specific examples include diphenyl carbonate, bis (chlorophenyl) carbonate, m-cresyl carbonate, dinaphthyl carbonate, bis (p-butylphenyl) carbonate, dimethyl carbonate, diethyl carbonate, and dibutyl carbonate. preferable.

  The carbonic acid diester is preferably mixed so as to have a molar ratio of 1.02 to 0.98 with respect to the total ether diol compound, more preferably 1.01 to 0.98, and still more preferably 1.01 to 0.98. 0.99. If the molar ratio of the carbonic acid diester is more than 1.02, the carbonic acid ester residue acts as a terminal block and a sufficient degree of polymerization cannot be obtained, which is not preferable. Even when the molar ratio of carbonic acid diester is less than 0.98, a sufficient degree of polymerization cannot be obtained, which is not preferable.

  A catalyst deactivator can also be added to the polycarbonate resin (component A-1) obtained by the above production method. As the catalyst deactivator, known catalyst deactivators are effectively used. Among them, ammonium salts and phosphonium salts of sulfonic acid are preferable, and further, dodecylbenzenesulfonic acid such as tetrabutylphosphonium salt of dodecylbenzenesulfonic acid is preferable. The salts of paratoluenesulfonic acid such as the above-mentioned salts and paratoluenesulfonic acid tetrabutylammonium salt are preferred. As esters of sulfonic acid, methyl benzenesulfonate, ethyl benzenesulfonate, butyl benzenesulfonate, octyl benzenesulfonate, phenyl benzenesulfonate, methyl paratoluenesulfonate, ethyl paratoluenesulfonate, butyl paratoluenesulfonate, para Octyl toluenesulfonate, phenyl p-toluenesulfonate and the like are preferably used, and among them, tetrabutylphosphonium dodecylbenzenesulfonate is most preferably used. These catalyst deactivators are used in an amount of 0.5 to 50 mol, preferably 0.5 to 10 mol, per mol of the polymerization catalyst selected from alkali metal compounds and / or alkaline earth metal compounds. It can be used in a proportion, more preferably in a proportion of 0.8 to 5 mol.

  The constituent resin (component A) of the present invention may contain another thermoplastic resin (component A-2) in addition to the polycarbonate resin (component A-1). As described above, the other resin (component A-2) is 50% by weight or less in the component A, preferably 40% by weight or less, more preferably 30% by weight or less, still more preferably 20% by weight or less, and particularly preferably 10% by weight. % Or less.

  As the thermoplastic resin as the component A-2, polyester resin (PEst), polyphenylene ether resin (PPE), polycarbonate resin (PC), polyamide resin (PA), polyolefin resin (PO), styrene resin, polyphenylene sulfide resin Examples thereof include at least one selected from the group consisting of (PPS) and polyetherimide resin (PEI). Of these A-2 components, polyester resin (PEst), polyphenylene ether resin (PPE), polycarbonate resin (PC), polyamide resin (PA), polyolefin resin (PO), and styrenic resin are preferable.

Next, the thermoplastic resin as the component A-2 will be specifically described.
As a polyester resin (PEst) as A-2 component, the 1 type, or 2 or more types of mixture selected from an aromatic polyester resin or an aliphatic polyester resin is mentioned. Preferred is an aromatic polyester resin, which is a polyester having an aromatic dicarboxylic acid as a main dicarboxylic acid component and an aliphatic diol having 2 to 10 carbon atoms as a main glycol component. Preferably 80 mol% or more, more preferably 90 mol% or more of the dicarboxylic acid component is composed of an aromatic dicarboxylic acid component. On the other hand, the glycol component preferably comprises an aliphatic diol component having 2 to 10 carbon atoms, more preferably 80 mol% or more, and more preferably 90 mol% or more.

  Preferable examples of the aromatic dicarboxylic acid component include terephthalic acid, isophthalic acid, phthalic acid, methyl terephthalic acid, methyl isophthalic acid, 2,6-naphthalenedicarboxylic acid, and the like. These can use 1 type (s) or 2 or more types. Examples of secondary dicarboxylic acids other than aromatic dicarboxylic acids include aliphatic dicarboxylic acids such as adipic acid, sebacic acid, decanedicarboxylic acid, azelaic acid, dodecanedicarboxylic acid, cyclohexanedicarboxylic acid, and alicyclic dicarboxylic acids. it can.

  Examples of the aliphatic diol having 2 to 10 carbon atoms include aliphatic diols such as ethylene glycol, trimethylene glycol, tetramethylene glycol, hexamethylene glycol and neopentyl glycol, and alicyclic diols such as 1,4-cyclohexanedimethanol. Can be mentioned. Examples of glycols other than aliphatic diols having 2 to 10 carbon atoms include p, p'-dihydroxyethoxybisphenol A and polyoxyethylene glycol.

  Preferred examples of the aromatic polyester resin include at least one dicarboxylic acid selected from terephthalic acid and 2,6-naphthalenedicarboxylic acid as the main dicarboxylic acid component, and ethylene glycol, trimethylene glycol, and tetramethylene as the main diol component. A polyester having an ester unit composed of at least one diol selected from glycols.

  Specific aromatic polyester resins include polyethylene terephthalate resin, polybutylene terephthalate resin, polyethylene naphthalate resin, polybutylene naphthalate resin, polycyclohexanedimethyl terephthalate resin, polytrimethylene terephthalate resin, and polytrimethylene naphthalate resin. It is preferably at least one selected from the group consisting of

  Particularly preferred is at least one selected from the group consisting of a polyethylene terephthalate resin, a polybutylene terephthalate resin and a polyethylene naphthalate resin. In particular, polybutylene terephthalate resin is particularly preferable.

  Moreover, the polyester elastomer which uses the said repeating unit as the main repeating unit of a hard segment can also be used as aromatic polyester resin of this invention.

As the soft segment of the polyester elastomer having tetramethylene terephthalate or tetramethylene-2,6-naphthalenedicarboxylate as the main repeating unit of the hard segment, for example, dicarboxylic acid is selected from terephthalic acid, isophthalic acid, sebacic acid and adipic acid From at least one dicarboxylic acid consisting of at least one dicarboxylic acid and having a diol component selected from the group consisting of a long-chain diol having 5 to 10 carbon atoms and H (OCH ₂ CH ₂ ) _i OH (i = 2 to 5) Further, a polyester or polycaprolactone having a melting point of 100 ° C. or lower or amorphous can be used.

  The main component is a component of 80 mol% or more, preferably 90 mol% or more of the total dicarboxylic acid component or the total glycol component, and the main repeating unit is 80 mol% or more of the total repeating unit, preferably 90 mol%. It is a repeating unit of mol% or more.

  The molecular weight of the aromatic polyester resin in the present invention may be any intrinsic viscosity that can be used as a normal molded article, and the intrinsic viscosity measured in orthochlorophenol at 35 ° C. is preferably 0.5 to 1.6 dl. / G, more preferably 0.6 to 1.5 dl / g.

  Moreover, it is advantageous that the aromatic polyester resin has a terminal carboxyl group (—COOH) amount of 1 to 60 equivalents / T (1 ton of polymer). The amount of the terminal carboxyl group can be determined, for example, by potentiometric titration of an m-cresol solution with an alkaline solution.

  As polyphenylene ether resin as A-2 component, what is generally known as PPE resin can be used. Specific examples of such PPE include (2,6-dimethyl-1,4-phenylene) ether, (2,6-diethyl-1,4-phenylene) ether, (2,6-dipropyl-1,4-phenylene). ) Ether, (2-methyl-6-ethyl-1,4-phenylene) ether, (2-methyl-6-propyl-1,4-phenylene) ether, (2,3,6-trimethyl-1,4- Homopolymers and / or copolymers such as (phenylene) ether are mentioned, and poly (2,6-dimethyl-1,4-phenylene) ether is particularly preferred. Moreover, the copolymer which the styrene compound graft-polymerized to these PPE may be sufficient. The method for producing such PPE is not particularly limited. For example, 2,6-xylenol is oxidized using a complex of cuprous salt and amines as a catalyst according to the method described in US Pat. No. 3,306,874. It can be easily produced by polymerization.

  The reduced viscosity ηsp / C (0.5 g / dl, toluene solution, measured at 30 ° C.), which is a measure of the molecular weight of the PPE resin, is 0.2 to 0.7 dl / g, preferably 0.3 to 0.6 dl. / G. A PPE resin having a reduced viscosity in this range has a good balance between molding processability and mechanical properties, and the reduced viscosity can be easily adjusted by adjusting the amount of catalyst during the production of PPE.

  The polycarbonate resin (PC) as the component A-2 is obtained by an interfacial polymerization reaction of various dihydroxyaryl compounds and phosgene using a solvent such as methylene chloride, or an ester of a dihydroxyaryl compound and diphenyl carbonate. What is obtained by an exchange reaction is mentioned. A typical example is a polycarbonate obtained by the reaction of 2,2'-bis (4-hydroxyphenyl) propane and phosgene.

  Examples of the dihydroxyaryl compound used as a raw material for polycarbonate include bis (4-hydroxyphenyl) methane, 1,1′-bis (4-hydroxyphenyl) ethane, 2,2′-bis (4-hydroxyphenyl) propane, 2, 2'-bis (4-hydroxyphenyl) butane, 2,2'-bis (4-hydroxyphenyl) octane, 2,2'-bis (4-hydroxy-3-methylphenyl) propane, 2,2'-bis (4-hydroxy-3-tert-butylphenyl) propane, 2,2′-bis (3,5-dimethyl-4-hydroxyphenyl) propane, 2,2′-bis (4-hydroxy-3-cyclohexylphenyl) Propane, 2,2′-bis (4-hydroxy-3-methoxyphenyl) propane, 1,1′-bis (4-hydroxyphenyl) Cyclopentane, 1,1′-bis (4-hydroxyphenyl) cyclohexane, 1,1′-bis (4-hydroxyphenyl) cyclododecane, 4,4′-dihydroxyphenyl ether, 4,4′-dihydroxy-3, 3'-dimethylphenyl ether, 4,4'-dihydroxydiphenyl sulfide, 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfide, 4,4'-dihydroxydiphenyl sulfoxide, 4,4'-dihydroxydiphenyl sulfone, Examples include bis (4-hydroxyphenyl) ketone. These dihydroxyaryl compounds can be used alone or in combination of two or more.

  Preferred dihydroxyaryl compounds include bisphenols that form highly heat-resistant aromatic polycarbonates, bis (hydroxyphenyl) alkanes such as 2,2′-bis (4-hydroxyphenyl) propane, and bis (4-hydroxyphenyl) cyclohexane. Bis (hydroxyphenyl) cycloalkane, dihydroxydiphenyl sulfide, dihydroxydiphenyl sulfone, dihydroxydiphenyl ketone and the like. A particularly preferred dihydroxyaryl compound is 2,2'-bis (4-hydroxyphenyl) propane which forms a bisphenol A type aromatic polycarbonate.

  In addition, if it is a range which does not impair heat resistance, mechanical strength, etc., when manufacturing bisphenol A type aromatic polycarbonate, you may substitute a part of bisphenol A with another dihydroxyaryl compound.

The molecular weight of the polycarbonate resin is not particularly limited, but if it is too low, the strength is not sufficient, and if it is too high, the melt viscosity becomes high and it becomes difficult to mold, so it is usually 10,000 to 50,000 in terms of viscosity average molecular weight. It is preferably 15,000 to 30,000. The viscosity average molecular weight (M) mentioned here is obtained by inserting the specific viscosity (η _sp ) obtained from a solution obtained by dissolving 0.7 g of polycarbonate resin in 100 ml of methylene chloride at 20 ° C. into the following equation.
η _sp /C=[η]+0.45×[η] ² C
[Η] = 1.23 × 10 ⁻⁴ M ^0.83
([Η] is the intrinsic viscosity, C is the polymer concentration of 0.7)

  The basic means for producing the polycarbonate resin will be briefly described. In the interfacial polymerization method (solution polymerization method) using phosgene as a carbonate precursor, the reaction is usually performed in the presence of an acid binder and an organic solvent. Examples of the acid binder include alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, or amine compounds such as pyridine. As the organic solvent, for example, halogenated hydrocarbons such as methylene chloride and chlorobenzene are used. In addition, a catalyst such as a tertiary amine or a quaternary ammonium salt can be used for promoting the reaction, and a terminal terminator such as an alkyl-substituted phenol such as phenol or p-tert-butylphenol is used as a molecular weight regulator. It is desirable to use it. The reaction temperature is preferably 0 to 40 ° C., the reaction time is several minutes to 5 hours, and the pH during the reaction is preferably maintained at 10 or more. It should be noted that not all of the resulting molecular chain ends need to have a structure derived from a terminal terminator.

  In a transesterification reaction (melt polymerization method) using a carbonic acid diester as a carbonate precursor, a predetermined proportion of dihydric phenol is stirred with the carbonic acid diester in the presence of an inert gas, and the resulting alcohol or phenol is distilled. It is done by the method. The reaction temperature varies depending on the boiling point of the alcohol or phenol produced, but is usually in the range of 120 to 350 ° C. The reaction is completed while distilling off the alcohol or phenol produced under reduced pressure from the beginning. An end terminator is added simultaneously with the dihydric phenol or the like in the initial stage of the reaction or in the middle of the reaction. Moreover, in order to accelerate | stimulate reaction, the catalyst used for the transesterification reaction now well-known can be used. Examples of the carbonic acid diester used in the transesterification include diphenyl carbonate, dinaphthyl carbonate, dimethyl carbonate, diethyl carbonate, and dibutyl carbonate. Of these, diphenyl carbonate is particularly preferred.

  Examples of the polyamide resin (PA) as the component A-2 include ring-opening polymer of cyclic lactam, polymer of aminocarboxylic acid, polycondensate of dibasic acid and diamine, and the like. Nylon 6, Nylon 66, Nylon 46, Nylon 610, Nylon 612, Nylon 11, Nylon 12, and other aliphatic polyamides and poly (metaxylene adipamide), poly (hexamethylene terephthalamide), poly (nonamethylene terephthalamide) And aliphatic-aromatic polyamides such as poly (hexamethylene isophthalamide) and poly (tetramethylene isophthalamide), and copolymers and mixtures thereof. The polyamide that can be used in the present invention is not particularly limited.

  The molecular weight of such a polyamide resin is not particularly limited, but a relative viscosity of 1.7 to 4.5 measured at 25% in 98% sulfuric acid at a concentration of 1% can be preferably used. Is 2.0 to 4.0, particularly preferably 2.0 to 3.5.

  The polyolefin resin as the component A-2 is a homopolymer or copolymer of olefins such as ethylene, propylene and butene, or a copolymer of monomer components copolymerizable with these olefins. . Specifically, polyethylene, polypropylene, ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate copolymer, ethylene-acrylic acid copolymer, ethylene-methyl methacrylate copolymer, ethylene-α-olefin copolymer Examples thereof include a copolymer, an ethylene-propylene copolymer, and an ethylene-butene copolymer. The molecular weight of these polyolefin resins is not particularly limited, but the higher the molecular weight, the better the flame retardancy.

  The styrene resin as the component A-2 is a homopolymer or copolymer of an aromatic vinyl monomer such as styrene, α-methylstyrene or vinyltoluene, these monomers and acrylonitrile, methyl methacrylate or the like. Styrene and / or styrene derivatives, or styrene and / or styrene derivatives and other vinyl monomers are graft-polymerized onto copolymers with vinyl monomers, diene rubbers such as polybutadiene, ethylene / propylene rubber, acrylic rubber, etc. It has been made. Specific examples of the styrenic resin include, for example, polystyrene, high-impact polystyrene (HIPS), acrylonitrile / styrene copolymer (AS resin), acrylonitrile / butadiene / styrene copolymer (ABS resin), methyl methacrylate / butadiene / styrene. Copolymer (MBS resin), Methyl methacrylate / Acrylonitrile / Butadiene / Styrene copolymer (MABS resin), Acrylonitrile / Acrylic rubber / Styrene copolymer (AAS resin), Acrylonitrile / Ethylene propylene rubber / Styrene copolymer (ABS resin) AES resin) or a mixture thereof. From the viewpoint of impact resistance, a rubber-modified styrene resin is preferable, and the rubber-modified styrene resin refers to a polymer in which a rubber-like polymer is dispersed in a particle form in a matrix made of a vinyl aromatic polymer. Aromatic vinyl monomer in the presence of rubbery polymer, and optionally vinyl monomer are added to obtain a monomer mixture by known block polymerization, block suspension polymerization, solution polymerization or emulsion polymerization. It is done.

  Examples of the rubber-like polymer include diene rubbers such as polybutadiene, poly (styrene-butadiene), poly (acrylonitrile-butadiene), and saturated rubbers obtained by hydrogenation of the diene rubber, isoprene rubber, chloroprene rubber, polybutyl acrylate. Examples thereof include acrylic rubbers such as ethylene-propylene-diene terpolymer (EPDM), and diene rubbers are particularly preferable.

  The aromatic vinyl monomer as an essential component in the graft copolymerizable monomer mixture to be polymerized in the presence of the rubbery polymer is, for example, styrene, α-methylstyrene, paramethylstyrene, and the like. Styrene is most preferred.

  Examples of vinyl monomers that can be added as needed include acrylonitrile and methyl methacrylate.

  The rubber-like polymer in the rubber-modified styrene resin is 1 to 50% by weight, preferably 2 to 40% by weight. The monomer mixture capable of graft polymerization is 99 to 50% by weight, preferably 98 to 60% by weight.

式中、ｎは１以上の整数であり、５０〜５００の整数が好ましく１００〜４００の整数がより好ましく、直鎖状、架橋状いずれであってもよい。 The polyphenylene sulfide resin (PPS) as the component A-2 has a repeating unit represented by the following formula.

In the formula, n is an integer of 1 or more, preferably an integer of 50 to 500, more preferably an integer of 100 to 400, and may be linear or crosslinked.

  An example of a method for producing a polyphenylene sulfide resin is a method of reacting dichlorobenzene with sodium disulfide. Cross-linked polymers can be manufactured by polymerizing a polymer with a low polymerization degree in the presence of air and then partially crosslinking to increase the molecular weight. It can be manufactured by the method.

The polyetherimide resin (PEI) as the component A-2 has a repeating unit represented by the following formula.

Ar ¹ in the formula represents an aromatic dihydroxy compound residue, and Ar ² represents an aromatic diamine residue. As an aromatic dihydroxy compound, the aromatic dihydroxy compound shown by description of polycarbonate resin mentioned above is mentioned, Bisphenol A is especially preferable. As aromatic diamines, m-phenylenediamine, p-phenylenediamine, 4,4′-diaminodiphenyl, 3,4′-diaminodiphenyl, 4,4′-diaminodiphenyl ether, 3,4′-diaminodiphenyl ether, diaminodiphenylmethane, Examples include diaminodiphenyl sulfone and diaminodiphenyl sulfide.
N in the above formula represents an integer of 5 to 1,000, and an integer of 10 to 500 is preferable.

  Examples of the method for producing the polyetherimide resin include US Pat. No. 3,847,867, US Pat. No. 3,847,869, US Pat. No. 3,850,885, US Pat. No. 3,852. 242 and U.S. Pat. No. 3,855,178.

  Of the various A-2 components described above, polyester resin (PEst), polyphenylene ether resin (PPE), polycarbonate resin (PC), polyamide resin (PA) or styrene resin is preferred.

（式中、Ｘ^１、Ｘ^２は同一もしくは異なり、下記式（２）で表される芳香族置換アルキル基である。） In the present invention, the organophosphorus compound used as the component B is represented by the following formula (1).

(In formula, X < ¹ >, X < ² > is the same or different, and is an aromatic substituted alkyl group represented by following formula (2).)

（式中、ＡＬは炭素数１〜５の分岐状または直鎖状の脂肪族炭化水素基であり、Ａｒは置換基を有しても良いフェニル基、ナフチル基、またはアントリル基である。ｎは１〜３の整数を示し、ＡｒはＡＬ中の任意の炭素原子に結合することができる。）

(In the formula, AL is a branched or linear aliphatic hydrocarbon group having 1 to 5 carbon atoms, and Ar is a phenyl group, a naphthyl group, or an anthryl group which may have a substituent. Represents an integer of 1 to 3, and Ar can be bonded to any carbon atom in AL.)

  Preferably, it is one or a mixture of two or more selected from the group consisting of organic phosphorus compounds represented by the following formulas (3) and (4).

（式中、Ｒ^２、Ｒ^５は同一または異なっていてもよく、置換基を有しても良いフェニル基、ナフチル基、またはアントリル基である。Ｒ^１、Ｒ^３、Ｒ^４、Ｒ^６は同一または異なっていてもよく、水素原子、炭素数１〜４の分岐状または直鎖状のアルキル基、置換基を有しても良いフェニル基、ナフチル基、またはアントリル基から選択される置換基である。）

(In the formula, R ² and R ⁵ may be the same or different, and may be a phenyl group, a naphthyl group, or an anthryl group that may have a substituent. R ¹ , R ³ , R ⁴ , R ⁶ are Substituents which may be the same or different and are selected from a hydrogen atom, a branched or straight chain alkyl group having 1 to 4 carbon atoms, an optionally substituted phenyl group, naphthyl group, or anthryl group .)

（式中、Ａｒ^１およびＡｒ^２は、同一又は異なっていても良く、フェニル基、ナフチル基またはアントリル基であり、その芳香環に置換基を有していてもよい。Ｒ^１１、Ｒ^１２、Ｒ^１３およびＲ^１４は、同一又は異なっていても良く、水素原子、炭素数１〜３の脂肪族炭化水素基またはフェニル基、ナフチル基もしくはアントリル基であり、その芳香環に置換基を有していてもよい。ＡＬ^１およびＡＬ^２は、同一又は異なっていても良く、炭素数１〜４の分岐状または直鎖状の脂肪族炭化水素基である。Ａｒ^３およびＡｒ^４は、同一又は異なっていても良く、フェニル基、ナフチル基またはアントリル基であり、その芳香環に置換基を有していてもよい。ｐおよびｑは０〜３の整数を示し、Ａｒ^３およびＡｒ^４はそれぞれＡＬ^１およびＡＬ^２の任意の炭素原子に結合することができる。）

(In formula, Ar < ¹ > and Ar < ² > may be the same or different, and are a phenyl group, a naphthyl group, or an anthryl group, and may have a substituent in the aromatic ring. R < ¹¹ >, R < ¹² >, R ¹³ and R ¹⁴ may be the same or different, and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 3 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, and have a substituent in the aromatic ring. AL ¹ and AL ² may be the same or different and are branched or straight-chain aliphatic hydrocarbon groups having 1 to 4 carbon atoms, Ar ³ and Ar ⁴ may be the same or It may be different, and may be a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring, p and q each represent an integer of 0 to ^3, and Ar ³ and Ar ⁴ each represent AL ¹ Contact It can be attached to any carbon atom of the fine AL ^2.)

  Furthermore, it is preferably a phosphorus compound represented by the following formulas (5), (6), (7), (8).

In the formula, R ²¹ and R ²² are the same or different and are a phenyl group, a naphthyl group or an anthryl group which may have a substituent on the aromatic ring, and among them, a phenyl group is preferable. The phenyl group, naphthyl group or anthryl group of R ²¹ and R ²² may be substituted with a hydrogen atom of the aromatic ring, and as a substituent, methyl, ethyl, propyl, butyl or a bonding group of the aromatic ring is Examples thereof include an aryl group having 6 to 14 carbon atoms via an oxygen atom, a sulfur atom, or an aliphatic hydrocarbon group having 1 to 4 carbon atoms.

In the above formula (6), R ³¹ and R ³⁴ may be the same or different and are a hydrogen atom or an aliphatic hydrocarbon group having 1 to 4 carbon atoms. Preferred are a hydrogen atom, a methyl group, and an ethyl group, and particularly preferred is a hydrogen atom. R ³³ and R ³⁶ may be the same or different and are each an aliphatic hydrocarbon group having 1 to 4 carbon atoms, preferably a methyl group or an ethyl group. R ³² and R ³⁵ may be the same or different, and are a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring. Preferably, it represents a phenyl group, and may have a substituent in any part other than the part bonded to phosphorus via a carbon atom on the aromatic ring, and includes methyl, ethyl, propyl (including isomers) , Butyl (including isomers) or a group bonded to the aromatic ring thereof is an aryl group having 6 to 14 carbon atoms via oxygen, sulfur or an aliphatic hydrocarbon group having 1 to 4 carbon atoms.

In the above formula (6), preferred specific examples of R ³² and R ³⁵ include phenyl group, cresyl group, xylyl group, trimethylphenyl group, 4-phenoxyphenyl group, cumyl group, naphthyl group, 4-benzylphenyl group and the like. In particular, a phenyl group is preferable.

In the above formula (7), Ar ¹ and Ar ² may be the same or different, and are a phenyl group, a naphthyl group, or an anthryl group, and may have a substituent on the aromatic ring. R ¹¹ , R ¹² , R ¹³ and R ¹⁴ may be the same or different and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 3 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, and its aromatic ring May have a substituent. Preferably, it represents a phenyl group, and may have a substituent in any part other than the part bonded to phosphorus via a carbon atom on the aromatic ring, and includes methyl, ethyl, propyl (including isomers) , Butyl (including isomers) or a group bonded to the aromatic ring thereof is an aryl group having 6 to 14 carbon atoms via oxygen, sulfur or an aliphatic hydrocarbon group having 1 to 4 carbon atoms.

In the above formula (7), preferred specific examples of Ar ¹ and Ar ² include phenyl group, cresyl group, xylyl group, trimethylphenyl group, 4-phenoxyphenyl group, cumyl group, naphthyl group, 4-benzylphenyl group and the like. In particular, a phenyl group is preferable.

In the above formula (7), AL ¹ and AL ² may be the same or different and are branched or straight-chain aliphatic hydrocarbon groups having 1 to 4 carbon atoms. A branched or straight chain aliphatic hydrocarbon group having 1 to 3 carbon atoms is preferable, and a branched or straight chain aliphatic hydrocarbon group having 1 to 2 carbon atoms is particularly preferable.

In the above formula (7), preferred specific examples of AL ¹ and AL ² include a methylene group, an ethylene group, an ethylidene group, a trimethylene group, a propylidene group, an isopropylidene group, and the like. In particular, a methylene group, an ethylene group, and Ethylidene groups are preferred.

In the above formula (7), Ar ³ and Ar ⁴ may be the same or different, and are a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring. Preferably, it represents a phenyl group, and may have a substituent in any part other than the part bonded to phosphorus via a carbon atom on the aromatic ring, and includes methyl, ethyl, propyl (including isomers) , Butyl (including isomers) or a group bonded to the aromatic ring thereof is an aryl group having 6 to 14 carbon atoms via oxygen, sulfur or an aliphatic hydrocarbon group having 1 to 4 carbon atoms.

In the above formula (7), p and q is an integer of 0 to 3, Ar ³ and Ar ⁴ may be bonded to any carbon atoms of AL ¹ and AL ^2, respectively. p and q are preferably 0 or 1, particularly preferably 0.

In the above formula (8), R ⁴¹ and R ⁴⁴ may be the same or different and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 4 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, The ring may have a substituent. Preferably they are a hydrogen atom, a C1-C3 aliphatic hydrocarbon group, or a phenyl group which may have a substituent. When R ⁴¹ and R ⁴⁴ are phenyl groups, they may have a substituent in any part other than the part bonded to phosphorus via a carbon atom on the aromatic ring, and methyl, ethyl, propyl (isomer The linking group to the aromatic ring is oxygen, sulfur or an aryl group having 6 to 14 carbon atoms via an aliphatic hydrocarbon group having 1 to 4 carbon atoms. .

In the above formula (8), preferred examples of R ⁴¹ and R ⁴⁴ include hydrogen atom, methyl group, ethyl group, propyl group (including isomers), phenyl group, cresyl group, xylyl group, trimethylphenyl group, A 4-phenoxyphenyl group, a cumyl group, a naphthyl group, a 4-benzylphenyl group, and the like can be given. A hydrogen atom, a methyl group, or a phenyl group is particularly preferable.

R ⁴² , R ⁴³ , R ⁴⁵ and R ⁴⁶ may be the same or different and are a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring. Preferably, it represents a phenyl group and may have a substituent in any part other than the part bonded to phosphorus via a carbon atom on the aromatic ring, and includes methyl, ethyl, propyl (including isomers) ), Butyl (including isomers) or a group bonded to the aromatic ring thereof is an aryl group having 6 to 14 carbon atoms via oxygen, sulfur or an aliphatic hydrocarbon group having 1 to 4 carbon atoms.

In the above formula (8), preferred specific examples of R ⁴² , R ⁴³ , R ⁴⁵ and R ⁴⁶ include phenyl group, cresyl group, xylyl group, trimethylphenyl group, 4-phenoxyphenyl group, cumyl group, naphthyl group, 4-benzylphenyl group etc. are mentioned, A phenyl group is especially preferable.

  The organophosphorus compound (component B) represented by the formula (1) exhibits a very excellent flame retardant effect for the resin. As far as the present inventors know, in the conventional flame-retarding of the resin by halogen-free, it is difficult to flame-retardant with a small amount of flame retardant, and there are many problems in practical use.

  However, according to the present invention, surprisingly, the organophosphorus compound (component B) can be easily made flame retardant by itself in a small amount, and does not impair the original properties of the resin.

  However, in the present invention, in addition to the B component, a phosphorus compound other than the B component, a fluorine-containing resin or other additive is used to reduce the use ratio of the B component, improve the flame retardancy of the molded product, and the physical properties of the molded product. Naturally, it can be added for the purpose of improving the chemical properties of molded articles, improving the chemical properties of molded articles, or other purposes. These other blending components will be specifically described later.

  The organophosphorus compound (component B) as a flame retardant in the flame retardant resin composition of the present invention is represented by the above formula (1), but the most preferred representative compounds are the following formulas (1-a), (1 -B), (1-c) and (1-d).

Next, a method for synthesizing the organophosphorus compound (component B) in the present invention will be described. The component B may be produced by a method other than the method described below.
The component B can be obtained, for example, by reacting pentaerythritol with phosphorus trichloride, subsequently treating the oxidized reaction product with an alkali metal compound such as sodium methoxide, and then reacting with aralkyl halide.

  It can also be obtained by reacting pentaerythritol with aralkyl phosphonic acid dichloride, or reacting pentaerythritol with phosphorus trichloride and reacting aralkyl alcohol with a compound obtained by reacting pentaerythritol with phosphorus trichloride, followed by Arbuzov transfer at high temperature. . The latter reaction is disclosed, for example, in U.S. Pat. No. 3,141,032, JP-A-54-157156, and JP-A-53-39698.

The specific synthesis method of the B component will be described below. This synthesis method is merely for the purpose of explanation, and the B component used in the present invention is not limited to these synthesis methods, but also its modifications and other synthesis methods. It may be synthesized. A more specific synthesis method will be described in the preparation examples described later.
(I) the organophosphorus compound of (1-a) in component B;
A reaction product obtained by reacting pentaerythritol with phosphorus trichloride and then oxidizing with tertiary butanol can be obtained by treating with sodium methoxide and reacting with benzyl bromide.
(II) the organophosphorus compound of (1-b) in component B;
A reaction product obtained by reacting pentaerythritol with phosphorus trichloride and then oxidizing with tertiary butanol can be obtained by treating with sodium methoxide and reacting with 1-phenylethyl bromide.
(III) the organophosphorus compound of (1-c) in component B;
A reaction product obtained by reacting pentaerythritol with phosphorus trichloride and then oxidizing with tertiary butanol can be obtained by treating with sodium methoxide and reacting with 2-phenylethyl bromide.
(IV) the organophosphorus compound of the above (1-d) in component B;
It can be obtained by reacting pentaerythritol with diphenylmethylphosphonic acid dichloride.

  Alternatively, it can be obtained by reacting pentaerythritol with phosphorus trichloride and heat-treating the resulting product and the reaction product of diphenylmethyl alcohol in the presence of a catalyst.

  As the above-mentioned B component, those having an acid value of 0.7 mgKOH / g or less, preferably 0.5 mgKOH / g or less are used. By using the component B having an acid value in this range, a molded product having excellent flame retardancy and hue can be obtained, and a molded product having good thermal stability can be obtained. The component B most preferably has an acid value of 0.4 mgKOH / g or less. Here, the acid value means the amount (mg) of KOH necessary for neutralizing the acid component in 1 g of the sample (component B).

  Furthermore, as the component B, one whose HPLC purity is preferably at least 90%, more preferably at least 95% is used. Such a high-purity product is preferable because of excellent flame retardancy, hue, and thermal stability of the molded product. Here, the HPLC purity of the B component can be measured effectively by using the following method.

  As the column, Develosil ODS-7 300 mm × 4 mmφ manufactured by Nomura Chemical Co., Ltd. was used, and the column temperature was 40 ° C. As a solvent, a mixed solution of acetonitrile and water 6: 4 (volume ratio) was used, and 5 μl was injected. The detector used was UV-260 nm.

  The method for removing impurities in component B is not particularly limited, but a method of performing repulp washing with a solvent such as water or methanol (washing with a solvent, repeating filtration several times) is the most effective. It is also advantageous in terms of cost.

  The B component is blended in an amount of 1 to 100 parts by weight, preferably 5 to 90 parts by weight, and more preferably 10 to 70 parts by weight with respect to 100 parts by weight of the resin component (component A). The suitable range of the blending ratio of the B component is determined by the desired flame retardancy level, the type of the resin component (A component), and the like. Even if it is other than component A and component B constituting these compositions, other components can be used as necessary as long as they do not impair the purpose of the present invention. Other flame retardants, flame retardant aids, fluorine-containing compounds The blending amount of the B component can be changed also by using the resin, and in many cases, the blending ratio of the B component can be reduced by using these resins.

  The flame-retardant resin composition of the present invention is prepared by adding a resin component (component A), an organophosphorus compound (component B) and other components as necessary, such as a V-type blender, super mixer, super floater, Henschel mixer, etc. A method of premixing using a mixer, supplying the premixture to a kneader, and melt mixing is preferably employed. As the kneader, various melt mixers such as a kneader, a single screw or a twin screw extruder can be used, and among these, the resin composition is 220 to 280 ° C., preferably 230 to 270 ° C. using the twin screw extruder. A method is preferably used in which a liquid component is injected by a side feeder, extruded by a side feeder, extruded, and pelletized by a pelletizer.

  The flame retardant resin composition of the present invention is substantially free of halogen and has very high flame retardant performance, such as home appliance parts, electrical / electronic parts, automobile parts, mechanical / mechanical parts, cosmetic containers, etc. It is useful as a material for molding various molded articles. Specifically, breaker parts, switch parts, motor parts, ignition coil cases, power plugs, power outlets, coil bobbins, connectors, relay cases, fuse cases, flyback transformer parts, focus block parts, distributor caps, harness connectors, etc. Can be suitably used. Furthermore, thinning housings, casings or chassis, such as electronic and electrical products (such as telephones, personal computers, printers, fax machines, copiers, televisions, VCRs, audio equipment and other home appliances / OA equipment, or parts thereof) Useful for housings, casings or chassis. In particular, it is also useful as a printer casing, fixing unit parts, and other machine / mechanical parts of home appliances and OA products such as fax machines that require particularly excellent heat resistance and flame retardancy.

  The molding method is not particularly limited, such as injection molding, blow molding, press molding, and the like, but it is preferably manufactured by injection molding a pellet-shaped resin composition using an injection molding machine.

The flame retardant resin composition of the present invention and a molded product formed therefrom have the following advantages compared to conventional resin compositions using plant-derived materials.
(I) A resin composition using a plant-derived raw material having high flame retardancy can be obtained without substantially using a halogen-containing flame retardant.
(Ii) Since the organophosphorus compound as a flame retardant has an excellent flame retardant effect on a resin using a plant-derived raw material, the V-2 level can be achieved even with a relatively small amount of use.
(Iii) Due to the structure and characteristics of the organophosphorus compound used as a flame retardant, the resin using the plant-derived raw material is hardly thermally deteriorated when molding the resin using the plant-derived raw material or when using the molded product. In addition, a resin composition having excellent thermal stability can be obtained. Therefore, a composition having excellent balance in flame retardancy, mechanical strength and thermal stability can be obtained.
(Iv) Since the organophosphorus compound as a flame retardant is colorless and compatible with a resin using a plant-derived raw material, a molded product excellent in transparency can be obtained.

EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples. The evaluation was performed by the following method.
(1) Flame retardancy (UL-94 evaluation)
Flame retardancy is evaluated using a test piece with a thickness of 1/16 inch (1.6 mm) according to the vertical flame test defined in UL-94 of the US UL standard as a flame retardant evaluation scale. It was. In all the test pieces, V-2 was extinguished within 30 seconds after the flame was removed, and not more than this evaluation standard was designated as notV.
(2) Acid value It measured based on JIS-K-3504.

Preparation Example 1
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dibenzyl-3,9-dioxide (FR-1) Thermometer, condenser, and dropping funnel The reaction vessel was charged with 816.9 g (6.0 mol) of pentaerythritol, 19.0 g (0.24 mol) of pyridine, and 2250.4 g (24.4 mol) of toluene and stirred. To the reaction vessel, 1651.8 g (12.0 mol) of phosphorus trichloride was added using the dropping funnel, and the mixture was heated and stirred at 60 ° C. after the addition was completed. After the reaction, the reaction mixture was cooled to room temperature, and 26.50 parts of methylene chloride was added to the resulting reaction product, and 889.4 g (12.0 moles) of tertiary butanol and 150.2 g (1.77 moles) of methylene chloride were cooled with ice. Mol) was added dropwise. The obtained crystals were washed with toluene and methylene chloride and filtered. The obtained filtered product was dried at 80 ° C. and 1.33 × 10 ² Pa for 12 hours to obtain 1341.1 g (5.88 mol) of a white solid. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide according to ³¹ P, ¹ HNMR spectrum. confirmed.

2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide obtained in a reaction vessel equipped with a thermometer, condenser and dropping funnel 1341.0 g (5.88 mol) and DMF6534.2 g (89.39 mol) were charged and stirred. Sodium methoxide 648.7 g (12.01 mol) was added to the reaction vessel under ice cooling. After stirring for 2 hours under ice cooling, the mixture was stirred for 5 hours at room temperature. After further distilling off DMF, 2613.7 g (35.76 mol) of DMF was added, and 2037.79 g (11.91 mol) of benzyl bromide was added dropwise to the reaction mixture under ice cooling. After stirring for 3 hours under ice cooling, DMF was distilled off, 8 L of water was added, and the precipitated solid was collected by filtration and washed twice with 2 L of water. The obtained crude product and 4 L of methanol were put into a reaction vessel equipped with a condenser and a stirrer and refluxed for about 2 hours. After cooling to room temperature, the crystals were separated by filtration, washed with 2 L of methanol, and the obtained filtered product was dried at 120 ° C. and 1.33 × 10 ² Pa for 19 hours to obtain 1863.5 g of white scaly crystals ( 4.56 mol) was obtained. The crystals obtained are ³¹ P, ¹ HNMR spectrum and elemental analysis with 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dibenzyl-3,9-dioxide. I confirmed it. The yield was 76% and ³¹ PNMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.06 mgKOH / g.
¹ H-NMR (DMSO-d ₆ , 300 MHz): δ 7.2-7.4 (m, 10H), 4.1-4.5 (m, 8H), 3.5 (d, 4H), ³¹ P _{-NMR (DMSO-d 6, 120MHz} ): δ23.1 (S), melting point: 255-256 ° C., elemental analysis: calculated: C, 55.89; H, 5.43 , measurement values: C, 56.24 H, 5.35

Preparation Example 2
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dibenzyl-3,9-dioxide (FR-2) Reaction with stirrer, thermometer, condenser In a container, 22,9-dibenzyloxy-2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane 22.55 g (0.055 mol), benzyl bromide 19.01 g (0.11 mol) ) And 33.54 g (0.32 mol) of xylene, and dry nitrogen was allowed to flow while stirring at room temperature. Next, heating was started in an oil bath, and the mixture was heated and stirred at a reflux temperature (about 130 ° C.) for 4 hours. After heating, the mixture was allowed to cool to room temperature, 20 mL of xylene was added, and the mixture was further stirred for 30 minutes. The precipitated crystals were separated by filtration and washed twice with 20 mL of xylene. The obtained crude product and 40 mL of methanol were placed in a reaction vessel equipped with a condenser and a stirrer and refluxed for about 2 hours. After cooling to room temperature, the crystals were separated by filtration and washed with 20 mL of methanol, and the obtained filtered product was dried at 120 ° C. and 1.33 × 10 ² Pa for 19 hours to obtain white scaly crystals. The product was confirmed to be bisbenzylpentaerythritol diphosphonate by mass spectral analysis, ¹ H, ³¹ P nuclear magnetic resonance spectral analysis and elemental analysis. The yield was 20.60 g, the yield was 91%, and ³¹ PNMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.05 mgKOH / g.
¹ H-NMR (DMSO-d ₆ , 300 MHz): δ 7.2-7.4 (m, 10H), 4.1-4.5 (m, 8H), 3.5 (d, 4H), ³¹ P _{-NMR (DMSO-d 6, 120MHz} ): δ23.1 (S), melting point: 257 ° C.

Preparation Example 3
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-diα-methylbenzyl-3,9-dioxide (FR-3) Thermometer, condenser, A reaction vessel equipped with a dropping funnel was charged with 816.9 g (6.0 mol) of pentaerythritol, 19.0 g (0.24 mol) of pyridine, and 2250.4 g (24.4 mol) of toluene and stirred. To the reaction vessel, 1651.8 g (12.0 mol) of phosphorus trichloride was added using the dropping funnel, and the mixture was heated and stirred at 60 ° C. after the addition was completed. After the reaction, the reaction mixture was cooled to room temperature, and 5180.7 g (61.0 mol) of methylene chloride was added to the obtained reaction product, and 889.4 g (12.0 mol) of tertiary butanol and 150. 2 g (1.77 mol) was added dropwise. The obtained crystals were washed with toluene and methylene chloride and filtered. The obtained filtered product was dried at 80 ° C. and 1.33 × 10 ² Pa for 12 hours to obtain 1341.1 g (5.88 mol) of a white solid. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide according to ³¹ P, ¹ HNMR spectrum. confirmed.

2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide obtained in a reaction vessel equipped with a thermometer, condenser and dropping funnel 1341.0 g (5.88 mol) and DMF6534.2 g (89.39 mol) were charged and stirred. Sodium methoxide 648.7 g (12.01 mol) was added to the reaction vessel under ice cooling. After stirring for 2 hours under ice cooling, the mixture was stirred for 5 hours at room temperature. After further distilling off DMF, 2613.7 g (35.76 mol) of DMF was added, and 2204.06 g (11.91 mol) of 1-phenylethyl bromide was added dropwise to the reaction mixture under ice cooling. After stirring for 3 hours under ice cooling, DMF was distilled off, 8 L of water was added, and the precipitated solid was collected by filtration and washed twice with 2 L of water. The obtained crude product and 4 L of methanol were put into a reaction vessel equipped with a condenser and a stirrer and refluxed for about 2 hours. After cooling to room temperature, the crystals were separated by filtration, washed with 2 L of methanol, and the obtained filtered product was dried at 120 ° C. and 1.33 × 10 ² Pa for 19 hours to obtain 1845.9 g of white scaly crystals ( 4.23 mol) was obtained. The obtained solid was analyzed by ³¹ PNMR, ¹ HNMR spectrum and elemental analysis, 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-diα-methylbenzyl-3,9. -Confirmed that it was a geoxide. ³¹ PNMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.03 mgKOH / g.

¹ H-NMR (CDCl ₃ , 300 MHz): δ 7.2-7.4 (m, 10H), 4.0-4.2 (m, 4H), 3.4-3.8 (m, 4H), 3.3 (qd, 4H), 1.6 (ddd, 6H), ³¹ P-NMR (CDCl ₃ , 120 MHz): δ 28.7 (S), melting point: 190-210 ° C., elemental analysis calculated value: C, 57.80; H, 6.01, measured value: C, 57.83; H, 5.96

Preparation Example 4
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-di (2-phenylethyl) -3,9-dioxide (FR-4) Thermometer A reaction vessel equipped with a condenser and a dropping funnel was charged with 816.9 g (6.0 mol) of pentaerythritol, 19.0 g (0.24 mol) of pyridine, and 2250.4 g (24.4 mol) of toluene and stirred. To the reaction vessel, 1651.8 g (12.0 mol) of phosphorus trichloride was added using the dropping funnel, and the mixture was heated and stirred at 60 ° C. after the addition was completed. After the reaction, the reaction mixture was cooled to room temperature, and 5180.7 g (61.0 mol) of methylene chloride was added to the obtained reaction product, and 889.4 g (12.0 mol) of tertiary butanol and 150. 2 g (1.77 mol) was added dropwise. The obtained crystals were washed with toluene and methylene chloride and filtered. The obtained filtered product was dried at 80 ° C. and 1.33 × 10 ² Pa for 12 hours to obtain 1341.1 g (5.88 mol) of a white solid. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide according to ³¹ P, ¹ HNMR spectrum. confirmed.

2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-dihydro-3,9-dioxide obtained in a reaction vessel equipped with a thermometer, condenser and dropping funnel 1341.0 g (5.88 mol) and DMF6534.2 g (89.39 mol) were charged and stirred. Sodium methoxide 648.7 g (12.01 mol) was added to the reaction vessel under ice cooling. After stirring for 2 hours under ice cooling, the mixture was stirred for 5 hours at room temperature. After further distilling off DMF, 2613.7 g (35.76 mol) of DMF was added, and 2183.8 g (11.8 mol) of (2-bromoethyl) benzene was added dropwise to the reaction mixture under ice cooling. After stirring for 3 hours under ice cooling, DMF was distilled off, 8 L of water was added, and the precipitated solid was collected by filtration and washed twice with 2 L of water. The obtained crude product and 4 L of methanol were put into a reaction vessel equipped with a condenser and a stirrer and refluxed for about 2 hours. After cooling to room temperature, the crystals were separated by filtration and washed with 2 L of methanol, and the resulting filtered product was dried at 120 ° C. and 1.33 × 10 ² Pa for 19 hours to give 1924.4 g (4. 41 mol) was obtained. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-di (2-phenylethyl) -3 by ³¹ PNMR, ¹ HNMR spectrum and elemental analysis. , 9-Dioxide was confirmed. ³¹ PNMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.03 mgKOH / g.

¹ H-NMR (CDCl ₃ , 300 MHz): δ 7.1-7.4 (m, 10H), 3.85-4.65 (m, 8H), 2.90-3.05 (m, 4H), 2.1-2.3 (m, 4H), ³¹ P-NMR (CDCl ₃ , 120 MHz): δ 31.5 (S), melting point: 245-246 ° C., elemental analysis calculated: C, 57.80; H , 6.01, measured value: C, 58.00; H, 6.07

Preparation Example 5
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-di (2-phenylethyl) -3,9-dioxide (FR-5) Stirrer, temperature In a reaction vessel having a total condenser, 3,9-di (2-phenylethoxy) -2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane 436.4 g (1.0 mol) Then, 370.1 g (2.0 mol) of 2-phenylethyl bromide was charged, and dry nitrogen was allowed to flow while stirring at room temperature. Next, heating was started in an oil bath, and the oil bath temperature was maintained at 180 ° C. for 10 hours. Thereafter, the oil bath was removed and the system was cooled to room temperature. To the obtained white solid reaction product, 2000 ml of methanol was added and washed with stirring, and then the white powder was filtered off using a glass filter. Next, the filtered white powder and 4000 ml of methanol were put into a reaction vessel equipped with a condenser and a stirrer and refluxed for about 2 hours. After cooling to room temperature, the crystals were separated by filtration and washed with 2000 mL of methanol. The obtained white powder was dried at 100 Pa and 120 ° C. for 8 hours to obtain 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-di (2-phenylethyl). 362.3 g of -3,9-dioxide was obtained. The product was bis 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-di (by mass spectral analysis, ¹ H, ³¹ P nuclear magnetic resonance spectral analysis and elemental analysis. 2-phenylethyl) -3,9-dioxide was confirmed. The yield was 83%, HPLC purity was 99.3%, and the acid value was 0.41 KOH mg / g.

¹ H-NMR (CDCl ₃ , 300 MHz): δ 7.1-7.4 (m, 10H), 3.85-4.65 (m, 8H), 2.90-3.05 (m, 4H), 2.1-2.3 (m, 4H), ³¹ P-NMR (CDCl ₃ , 120 MHz): δ 31.5 (S), melting point: 245-246 ° C.

Preparation Example 6
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-bis (diphenylmethyl) -3,9-dioxide (FR-6) Stirrer, stirrer In a 10-liter three-necked flask equipped with a reflux condenser and a thermometer, 2058.5 g (7.22 mol) of diphenylmethylphosphonic dichloride, 468.3 g (3.44 mol) of pentaerythritol, 1169.4 g of pyridine ( 14.8 mol) and 8200 g of chloroform were charged, heated to 60 ° C. under a nitrogen stream, and stirred for 6 hours. After completion of the reaction, chloroform was replaced with methylene chloride, 6 L of distilled water was added to the reaction mixture and stirred to precipitate a white powder. This was collected by suction filtration, and the obtained white product was washed with methanol and then dried at 100 ° C. and 1.33 × 10 ² Pa for 10 hours to obtain 1156.2 g of a white solid. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-bis (diphenylmethyl) by ³¹ P-NMR, ¹ H-NMR spectrum and elemental analysis. It was confirmed that it was −3,9-dioxide. ^{The 31} P-NMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.3 mgKOH / g.

¹ H-NMR (DMSO-d6, 300 MHz): δ 7.20-7.60 (m, 20H), 5.25 (d, 2H), 4.15-4.55 (m, 8H), ³¹ P- NMR (DMSO-d6, 120 MHz): δ 20.9, melting point: 265 ° C., elemental analysis calculated: C, 66.43; H, 5.39, measured: C, 66.14; H, 5.41

Preparation Example 7
Preparation of 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-bis (diphenylmethyl) -3,9-dioxide (FR-7) , A thermometer, and a condenser, and 40.4 g of 3,9-bis (diphenylmethoxy) -2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane was added to the flask under a nitrogen stream. (0.072 mol), 35.5 g (0.14 mol) of diphenylmethyl bromide and 48.0 g (0.45 mol) of xylene were added, and the mixture was heated and stirred at a reflux temperature (about 130 ° C.) for 3 hours. After heating, the mixture was allowed to cool to room temperature, 30 mL of xylene was added, and the mixture was further stirred for 30 minutes. The precipitated crystals were separated by filtration and washed twice with 30 mL of xylene. The obtained crude product and 100 mL of methanol were placed in an eggplant type flask, a condenser was attached, and the mixture was refluxed for about 1 hour. After cooling to room temperature, the crystals were separated by filtration, washed twice with 50 mL of methanol, and dried under reduced pressure at 120 ° C. The obtained solid was found to be 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane, 3,9-bis (diphenylmethyl) by ³¹ P-NMR, ¹ H-NMR spectrum and elemental analysis. It was confirmed that it was −3,9-dioxide. The obtained solid was a white powder, the yield was 36.8 g, and the yield was 91%. ³¹ PNMR purity was 99%. The HPLC purity measured by the method described in the text was 99%. The acid value was 0.07 mg KOH / g.

¹ H-NMR (DMSO-d ₆ , 300 MHz): δ 7.2-7.6 (m, 20H), 6.23 (d, J = 9 Hz, 2H), 3.89-4.36 (m, 6H) ), 3.38-3.46 (m, 2H), ³¹ P-NMR (CDCl ₃ , 120 MHz): δ 20.9 (S), melting point: 265 ° C., elemental analysis calculated: C, 66.43; H , 5.39, found: C, 66.14; H, 5.41

Preparation Example 8
Preparation of polycarbonate resin (PC-1) 7307 parts by weight (50 moles) of isosorbide and 10709 parts by weight (50 moles) of diphenyl carbonate were placed in a reactor, and 4.8 parts by weight (diphenyl) of tetramethylammonium hydroxide was used as a polymerization catalyst. 1 × 10 ⁻⁴ mol per 1 mol of carbonate component) and 5.0 × 10 ⁻³ parts by weight of sodium hydroxide (0.25 × 10 ⁻⁶ mol per mol of diphenyl carbonate component) It was melted by heating to 180 ° C. under atmospheric pressure and normal pressure.

Under stirring, the pressure in the reaction vessel was gradually reduced over 30 minutes, and the pressure was reduced to 13.3 × 10 ⁻³ MPa while the produced phenol was distilled off. After reacting in this state for 20 minutes, the temperature was raised to 200 ° C., then the pressure was gradually reduced over 20 minutes, and the reaction was carried out at 4.00 × 10 ⁻³ MPa for 20 minutes while distilling off the phenol. The mixture was heated to 250 ° C. for 30 minutes and reacted for 30 minutes.

Next, the pressure was gradually reduced, and the reaction was continued at 2.67 × 10 ⁻³ MPa for 10 minutes and 1.33 × 10 ⁻³ MPa for 10 minutes, and further reduced in pressure to reach 4.00 × 10 ⁻⁵ MPa. The temperature was gradually raised to 260 ° C., and the reaction was finally carried out at 260 ° C. and 6.66 × 10 ⁻⁵ MPa for 1 hour. The polymer after the reaction was pelletized to obtain a pellet having a specific viscosity of 0.33. The glass transition temperature of this pellet was 165 ° C., and the 5% weight loss temperature was 355 ° C.

Preparation Example 9
Preparation of polycarbonate resin (PC-2) Pellets having a specific viscosity of 0.23 were obtained in the same manner as in Reference Example 8 except that the reaction was finally performed at 255 ° C. and 6.66 × 10 ⁻⁵ MPa for 30 minutes. . The glass transition temperature of this pellet was 158 ° C., and the 5% weight loss temperature was 353 ° C.

Preparation Example 10
Preparation of polycarbonate resin (PC-3) Same as Reference Example 8 except that 6722 parts by weight (46 moles) of isosorbide, 10709 parts by weight (50 moles) of diphenyl carbonate and 304 parts by weight (4 moles) of 1,3-propanediol Thus, a pellet having a specific viscosity of 0.28 was obtained. The glass transition temperature of this pellet was 146 ° C., and the 5% weight loss temperature was 342 ° C.

The following were used for each component used in Examples and Comparative Examples.
(I) Polycarbonate resin (component A)
(I) Polycarbonate resin synthesized in Preparation Example 8 (hereinafter referred to as PC-1)
(Ii) Polycarbonate resin synthesized in Preparation Example 9 (hereinafter referred to as PC-2)
(Iii) Polycarbonate resin synthesized in Preparation Example 10 (hereinafter referred to as PC-3)
(II) Organophosphorus compound (component B)
(I) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-dibenzyl-3,9-dioxide synthesized in Preparation Example 1 {Formula (1-a) Phosphorus compound (hereinafter referred to as FR-1)}
(Ii) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-dibenzyl-3,9-dioxide synthesized in Preparation Example 2 {Formula (1-a) Phosphorus compound (hereinafter referred to as FR-2)}
(Iii) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-diα-methylbenzyl-3,9-dioxide synthesized in Preparation Example 3 {formula ( 1-b) phosphorus compound (hereinafter referred to as FR-3)}
(Iv) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-di (2-phenylethyl) -3,9-dioxide synthesized in Preparation Example 4 Phosphorus compound of formula (1-c) (hereinafter referred to as FR-4)}
(V) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-di (2-phenylethyl) -3,9-dioxide synthesized in Preparation Example 5 Phosphorus compound of formula (1-c) (hereinafter referred to as FR-5)}
(Vi) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-bis (diphenylmethyl) -3,9-dioxide synthesized in Preparation Example 6 {formula ( 1-d) phosphorus compound (hereinafter referred to as FR-6)}
(Vii) 2,4,8,10-tetraoxa-3,9-diphosphaspiro [5,5] undecane, 3,9-bis (diphenylmethyl) -3,9-dioxide synthesized in Preparation Example 7 {formula ( 1-d) phosphorus compound (hereinafter referred to as FR-7)}
(III) Other organophosphorus compounds (i) Triphenyl phosphate (TPP manufactured by Daihachi Chemical Industry Co., Ltd.) was used (hereinafter referred to as TPP).
(Ii) 1,3-phenylenebis [di (2,6-dimethylphenyl) phosphate] (PX-200 manufactured by Daihachi Chemical Industry Co., Ltd.) was used (hereinafter referred to as PX-200).

[Examples 1 to 21 and Comparative Examples 1 to 9]
Each component described in Tables 1 to 3 was blended with a tumbler in the amounts (parts by weight) described in Tables 1 to 3, and pelletized with a 15 mmφ twin screw extruder (manufactured by Technobel, KZW15). The obtained pellets were dried with a hot air dryer at 130 ° C. for 4 hours. The dried pellets were molded with an injection molding machine (J75EIII manufactured by Nippon Steel Works). The result evaluated using the shaping | molding board was shown to Tables 1-3.

Claims (16)

(A) With respect to 100 parts by weight of a resin component (component A) containing at least 50% by weight of a polycarbonate resin (component A-1) containing a carbonate constituent unit represented by the following formula (A-1), (B) A flame-retardant resin composition containing 1 to 100 parts by weight of an organic phosphorus compound (component B) represented by the following formula (1).

(In formula, X < ¹ >, X < ² > is the same or different, and is an aromatic substituted alkyl group represented by following formula (2).)

(In the formula, AL is a branched or linear aliphatic hydrocarbon group having 1 to 5 carbon atoms, and Ar is a phenyl group, a naphthyl group, or an anthryl group which may have a substituent. Represents an integer of 1 to 3, and Ar can be bonded to any carbon atom in AL.)   The flame retardancy according to claim 1, wherein the polycarbonate resin (component A-1) has a glass transition temperature (Tg) of 100 ° C to 165 ° C and a 5% weight loss temperature (Td) of 300 ° C to 400 ° C. Resin composition.   The flame retardant resin composition according to claim 1, wherein the carbonate constituent unit represented by the formula (A-1) is a carbonate constituent unit derived from isosorbide (1,4: 3,6-dianhydro-D-sorbitol). 2. The organophosphorus compound (component B) is one or a mixture of two or more selected from the group consisting of organophosphorus compounds represented by the following formulas (3) and (4). Flame retardant resin composition.

(In the formula, R ² and R ⁵ may be the same or different, and may be a phenyl group, a naphthyl group, or an anthryl group that may have a substituent. R ¹ , R ³ , R ⁴ , R ⁶ are Substituents which may be the same or different and are selected from a hydrogen atom, a branched or straight chain alkyl group having 1 to 4 carbon atoms, an optionally substituted phenyl group, naphthyl group, or anthryl group .)

(In formula, Ar < ¹ > and Ar < ² > may be the same or different, and are a phenyl group, a naphthyl group, or an anthryl group, and may have a substituent in the aromatic ring. R < ¹¹ >, R < ¹² >, R ¹³ and R ¹⁴ may be the same or different, and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 3 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, and have a substituent in the aromatic ring. AL ¹ and AL ² may be the same or different and are branched or straight-chain aliphatic hydrocarbon groups having 1 to 4 carbon atoms, Ar ³ and Ar ⁴ may be the same or It may be different, and may be a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring, p and q each represent an integer of 0 to ^3, and Ar ³ and Ar ⁴ each represent AL ¹ Contact It can be attached to any carbon atom of the fine AL ^2.) The flame retardant resin composition according to claim 1, wherein the organophosphorus compound (component B) is represented by the following formula (5).

(Wherein R ²¹ and R ²² are the same or different and are a phenyl group, a naphthyl group or an anthryl group, and the aromatic ring may have a substituent.) The flame retardant resin composition according to claim 1, wherein the organic phosphorus compound (component B) is a compound represented by the following formula (1-a).

The flame retardant resin composition according to claim 1, wherein the organic phosphorus compound (component B) is represented by the following formula (6).

(In the formula, R ³¹ and R ³⁴ may be the same or different, and are a hydrogen atom or an aliphatic hydrocarbon group having 1 to 3 carbon atoms. R ³³ and R ³⁶ may be the same or different. And an aliphatic hydrocarbon group having 1 to 4 carbon atoms, R ³² and R ³⁵ may be the same or different and each is a phenyl group, a naphthyl group or an anthryl group, and has a substituent in the aromatic ring. May be.) The flame retardant resin composition according to claim 1, wherein the organic phosphorus compound (component B) is a compound represented by the following formula (1-b).

The flame retardant resin composition according to claim 1, wherein the organophosphorus compound (component B) is represented by the following formula (7).

(In formula, Ar < ¹ > and Ar < ² > may be the same or different, and are a phenyl group, a naphthyl group, or an anthryl group, and may have a substituent in the aromatic ring. R < ¹¹ >, R < ¹² >, R ¹³ and R ¹⁴ may be the same or different, and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 3 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, and have a substituent in the aromatic ring. AL ¹ and AL ² may be the same or different and are branched or straight-chain aliphatic hydrocarbon groups having 1 to 4 carbon atoms, Ar ³ and Ar ⁴ may be the same or It may be different, and may be a phenyl group, a naphthyl group or an anthryl group, and may have a substituent on the aromatic ring, p and q each represent an integer of 0 to ^3, and Ar ³ and Ar ⁴ each represent AL ¹ Contact It can be attached to any carbon atom of the fine AL ^2.) The flame retardant resin composition according to claim 1, wherein the organic phosphorus compound (component B) is a compound represented by the following formula (1-c).

The flame retardant resin composition according to claim 1, wherein the organophosphorus compound (component B) is represented by the following formula (8).

(In the formula, R ⁴¹ and R ⁴⁴ may be the same or different and are a hydrogen atom, an aliphatic hydrocarbon group having 1 to 4 carbon atoms, a phenyl group, a naphthyl group or an anthryl group, and substituted on the aromatic ring thereof. R ⁴² , R ⁴³ , R ⁴⁵ and R ⁴⁶ may be the same or different and are a phenyl group, a naphthyl group or an anthryl group, and have a substituent on the aromatic ring. May be.) The flame retardant resin composition according to claim 1, wherein the organophosphorus compound (component B) is a compound represented by the following formula (1-d).

  The flame retardant resin composition according to claim 1, wherein the organic phosphorus compound (component B) has an acid value of 0.7 mg KOH / g or less.   The flame-retardant resin composition according to claim 1, wherein at least V-2 can be achieved at a flame-retardant level of UL-94 standard.   The flame-retardant resin composition according to claim 1, wherein the B component is contained in a proportion of 2 to 70 parts by weight with respect to 100 parts by weight of the A component.   A molded article formed from the flame retardant resin composition according to claim 1.