JP2740455B2 - Method for producing brominated polystyrene - Google Patents

Method for producing brominated polystyrene

Info

Publication number
JP2740455B2
JP2740455B2 JP6086619A JP8661994A JP2740455B2 JP 2740455 B2 JP2740455 B2 JP 2740455B2 JP 6086619 A JP6086619 A JP 6086619A JP 8661994 A JP8661994 A JP 8661994A JP 2740455 B2 JP2740455 B2 JP 2740455B2
Authority
JP
Japan
Prior art keywords
brominated polystyrene
polystyrene
bromination
present
powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP6086619A
Other languages
Japanese (ja)
Other versions
JPH07292026A (en
Inventor
晋一 門野
清志 三島
明久 高橋
▲あきら▼ 谷内
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Manac Inc
Original Assignee
Manac Inc
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Filing date
Publication date
Application filed by Manac Inc filed Critical Manac Inc
Priority to JP6086619A priority Critical patent/JP2740455B2/en
Publication of JPH07292026A publication Critical patent/JPH07292026A/en
Application granted granted Critical
Publication of JP2740455B2 publication Critical patent/JP2740455B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/18Introducing halogen atoms or halogen-containing groups

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、合成樹脂の難燃剤とし
て有用な臭素化ポリスチレンの製造方法に関する。
The present invention relates to a method for producing brominated polystyrene useful as a flame retardant for synthetic resins.

【0002】[0002]

【従来の技術】臭素化ポリスチレンは、飽和ポリエステ
ル、ポリアミドなどのエンジニアリングプラスチックを
代表とする各種合成樹脂の難燃剤として使用されおり、
これら難燃剤を配合した樹脂は、難燃化が必要な電気・
電子分野など各種分野で用いられている。
2. Description of the Related Art Brominated polystyrene is used as a flame retardant for various synthetic resins represented by engineering plastics such as saturated polyester and polyamide.
Resins containing these flame retardants are used in electrical and
It is used in various fields such as the electronic field.

【0003】臭素化ポリスチレンの製造方法は種々提案
されており、たとえば、特公平1−57684号公報に
は、重量平均分子量20000以上のポリスチレンを有
機溶媒中で、無水条件下に金属塩ルイス酸臭素化触媒の
存在下に、約50℃までの温度で塩化臭素と反応させる
臭素化ポリスチレンの製造方法、また、特開平2−21
5807号公報には、脱水剤の共存下、脂肪族ハロゲン
化炭化水素を溶媒として、ルイス酸触媒の存在下に、0
〜40℃でポリスチレンを臭素化する臭素化ポリスチレ
ンの製造方法が提案されている。しかしながら、これら
の方法はいずれも臭素化触媒としてルイス酸を使用して
いるため、無水条件又は少なくとも反応溶媒中の水分量
が0.02%以下で臭素化反応させることが必要であ
る。これ以上の水分が存在すると、ルイス酸触媒が分解
して臭素化が期待どおりに進まないため、難燃剤として
使用可能な高臭素含有率で耐熱性の優れた臭素化ポリス
チレンは得られない。また、ルイス酸触媒は空気中の水
分でも分解するため、保管には充分な管理が必要であ
る。このような点から、従来の製造法は工業的な製造方
法として満足できるものではなかった。
Various methods for producing brominated polystyrene have been proposed. For example, Japanese Patent Publication No. 1-57684 discloses polystyrene having a weight-average molecular weight of 20,000 or more in an organic solvent under a condition of anhydrous metal salt Lewis acid bromine. For producing brominated polystyrene by reacting with bromine chloride at a temperature of up to about 50 ° C. in the presence of a bromination catalyst;
Japanese Patent No. 5807 discloses that an aliphatic halogenated hydrocarbon is used in the presence of a Lewis acid catalyst in the presence of a Lewis acid catalyst in the presence of a dehydrating agent.
There has been proposed a method for producing brominated polystyrene in which polystyrene is brominated at ℃ 40 ° C. However, since all of these methods use a Lewis acid as a bromination catalyst, it is necessary to carry out the bromination reaction under anhydrous conditions or at least a water content of 0.02% or less in the reaction solvent. If more moisture is present, the Lewis acid catalyst decomposes and bromination does not proceed as expected, so that brominated polystyrene having a high bromine content and excellent heat resistance that can be used as a flame retardant cannot be obtained. In addition, since the Lewis acid catalyst is decomposed even by moisture in the air, sufficient control is required for storage. From such a point, the conventional production method was not satisfactory as an industrial production method.

【0004】[0004]

【発明が解決しようとする課題】本発明は、かかる問題
点を解決し、合成樹脂用難燃剤として優れた臭素化ポリ
スチレンを提供することを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to solve such problems and to provide brominated polystyrene which is excellent as a flame retardant for synthetic resins.

【0005】[0005]

【課題を解決するための手段】本発明者らは、かかる問
題点を解決するために鋭意検討を重ねた結果、ポリスチ
レンを臭素化する際に、触媒として酸化アンチモンを使
用することにより、含水条件下でも反応が進行し、得ら
れた臭素化ポリスチレンは色調、耐熱性が優れ、合成樹
脂用難燃剤として有用であることを見い出し、本発明に
到達した。
Means for Solving the Problems The inventors of the present invention have made intensive studies to solve the above-mentioned problems, and as a result, have found that the use of antimony oxide as a catalyst during the bromination of polystyrene allows the use of hydrous conditions. The reaction proceeded even below, and the resulting brominated polystyrene was found to be excellent in color tone and heat resistance, and was found to be useful as a flame retardant for synthetic resins, and reached the present invention.

【0006】すなわち、本発明は、ハロゲン化炭化水素
系溶媒に溶解又は分散させたポリスチレンを、酸化アン
チモン触媒の存在下に臭素化剤と反応させることを特徴
とする臭素化ポリスチレンの製造方法である。
That is, the present invention is a process for producing a brominated polystyrene, which comprises reacting polystyrene dissolved or dispersed in a halogenated hydrocarbon solvent with a brominating agent in the presence of an antimony oxide catalyst. .

【0007】以下、本発明を詳細に説明する。本発明の
臭素化に供するポリスチレンとしては、ポリスチレン、
スチレン−無水マレイン酸共重合体、ポリエチレン−ス
チレングラフト共重合体、スチレン−ブタジエン共重合
体、アクリロニトリル−スチレン共重合体、アクリロニ
トリル−ブタジエン−スチレン共重合体、スチレン−ジ
ビニルベンゼン架橋共重合体など少なくともスチレン成
分を50重量%以上含有するものが用いられる。また、
これらの発泡体、これらの回収品も使用することができ
る。
Hereinafter, the present invention will be described in detail. As polystyrene to be subjected to the bromination of the present invention, polystyrene,
Styrene-maleic anhydride copolymer, polyethylene-styrene graft copolymer, styrene-butadiene copolymer, acrylonitrile-styrene copolymer, acrylonitrile-butadiene-styrene copolymer, styrene-divinylbenzene cross-linked copolymer, etc. Those containing 50% by weight or more of a styrene component are used. Also,
These foams and their recovered products can also be used.

【0008】本発明で使用するハロゲン化炭化水素系溶
媒としては、塩化メチレン、クロロホルム、四塩化炭
素、エチレンジクロリド、1,1,1−トリクロロエタ
ン、トリクロロエチレン、テトラクロロエチレン、モノ
クロルベンゼンなどの塩素化炭化水素;臭化メチレン、
エチレンジブロミドなどの臭素化炭化水素が挙げられ
る。
The halogenated hydrocarbon solvents used in the present invention include chlorinated hydrocarbons such as methylene chloride, chloroform, carbon tetrachloride, ethylene dichloride, 1,1,1-trichloroethane, trichloroethylene, tetrachloroethylene and monochlorobenzene; Methylene bromide,
Brominated hydrocarbons such as ethylene dibromide.

【0009】本発明で使用する臭素化剤としては、臭素
又は塩化臭素を使用することができる。臭素化触媒であ
る酸化アンチモンとしては、三酸化二アンチモン、四酸
化二アンチモン、五酸化二アンチモンなどが用いられ
る。触媒の添加量はポリスチレン100重量部に対して
1〜30重量部であることが好ましい。
As the brominating agent used in the present invention, bromine or bromine chloride can be used. As antimony oxide which is a bromination catalyst, diantimony trioxide, diantimony tetroxide, diantimony pentoxide and the like are used. The amount of the catalyst to be added is preferably 1 to 30 parts by weight based on 100 parts by weight of polystyrene.

【0010】臭素化反応の際の水分含有量は、ルイス酸
触媒を使用する場合のように反応溶媒に対して0.02
%以下という実質的に無水状態である必要はない。好ま
しい水分含有量は反応溶媒に対して5%以下、さらに好
ましくは2%以下である。
The water content in the bromination reaction is 0.02 to the reaction solvent as in the case of using a Lewis acid catalyst.
% Need not be substantially anhydrous. The preferred water content is at most 5%, more preferably at most 2%, based on the reaction solvent.

【0011】本発明の臭素化反応は−20℃〜100℃
で行うことが好ましい。また、反応・熟成終了後に過剰
の臭素化剤を還元又は中和し、さらに水洗、中和したの
ち、得られた臭素化ポリスチレン溶液から反応溶媒を濃
縮留去するか、又は臭素化ポリスチレン溶液をメタノー
ルなどの貧溶剤中に加えることにより、臭素化ポリスチ
レンの固体又は粉体を得ることができる。
[0011] The bromination reaction of the present invention is carried out at a temperature of -20 ° C to 100 ° C.
It is preferable to carry out in. After completion of the reaction and aging, the excess brominating agent is reduced or neutralized, and further washed with water and neutralized, and then the reaction solvent is concentrated and distilled off from the obtained brominated polystyrene solution, or the brominated polystyrene solution is removed. By adding the compound in a poor solvent such as methanol, a solid or powder of brominated polystyrene can be obtained.

【0012】本発明の方法で得られた臭素化ポリスチレ
ンは、難燃剤として、熱可塑性樹脂、熱硬化性樹脂、熱
可塑性エラストマーなどの各種合成樹脂に配合すること
ができる。これら樹脂の例としては、ポリスチレン、ア
クリロニトリル−ブタジエン−スチレン共重合体などの
スチレン系樹脂;ポリエチレン、ポリプロピレンなどの
ポリオレフィン;ポリエチレンテレフタレート、ポリブ
チレンテレフタレートなどの飽和ポリエステル;ナイロ
ン66、ナイロン46などのポリアミド;変性ポリフェ
ニレンエーテルなどが挙げられる。
The brominated polystyrene obtained by the method of the present invention can be blended as a flame retardant with various synthetic resins such as thermoplastic resins, thermosetting resins, and thermoplastic elastomers. Examples of these resins include styrene resins such as polystyrene and acrylonitrile-butadiene-styrene copolymer; polyolefins such as polyethylene and polypropylene; saturated polyesters such as polyethylene terephthalate and polybutylene terephthalate; polyamides such as nylon 66 and nylon 46; Modified polyphenylene ether and the like can be mentioned.

【0013】[0013]

【実施例】以下に実施例を挙げて本発明を更に詳細に説
明するが、本発明はこれらの実施例によって限定される
ものではない。
EXAMPLES The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0014】実施例1 1L のガラス製反応器(撹拌装置、コンデンサー、温度
計、滴下ロートを備える)に、エチレンジクロリド(水
分0.002%)750gとポリスチレン(三菱化成ポ
リテックス製、商品名ダイヤレックス)75gを加え、
撹拌溶解したのち、三酸化二アンチモン11gを加え、
反応温度を10〜25℃に保ちつつ、予め調製しておい
た塩化臭素溶液(70重量%エチレンジクロリド溶液)
720gを滴下ロートより2時間かけて滴下した。滴下
終了後、内温を20〜30℃に保持して1時間熟成させ
た。熟成終了後、反応生成物を水洗したのち、有機層を
メタノール3L 中に滴下して晶析させた。結晶を濾過乾
燥後、臭素化ポリスチレンの粉体216gを得た。この
臭素化ポリスチレンの臭素含有率、TG(熱重量分
析)、外観色相及び加熱発生HBr量を以下に述べる方
法で測定した。分析結果を表1に示す。
Example 1 In a 1-liter glass reactor (provided with a stirrer, condenser, thermometer and dropping funnel), 750 g of ethylene dichloride (water content 0.002%) and polystyrene (Mitsubishi Kasei Polytex, trade name: Diamond) Rex) 75 g
After stirring and dissolving, 11 g of diantimony trioxide was added,
While maintaining the reaction temperature at 10 to 25 ° C., a bromine chloride solution prepared in advance (70% by weight ethylene dichloride solution)
720 g was dropped from the dropping funnel over 2 hours. After completion of the dropwise addition, the mixture was aged for 1 hour while maintaining the internal temperature at 20 to 30 ° C. After aging, the reaction product was washed with water, and the organic layer was dropped into 3 L of methanol for crystallization. After the crystals were filtered and dried, 216 g of brominated polystyrene powder was obtained. The bromine content, TG (thermogravimetric analysis), appearance hue, and heat-generated HBr amount of the brominated polystyrene were measured by the methods described below. Table 1 shows the analysis results.

【0015】・臭素含有率:JIS K 7299(フ
ラスコ燃焼法)に準じる方法で測定した。 ・TG(熱重量分析):示差熱測定装置(リガク製)を
使用し、空気雰囲気中、10℃/分の昇温速度で、室温
から700℃までの測定を行った。 ・外観色相:色彩色差計(ミノルタカメラ製 CR−1
00型)によって測定し、L、a、bの表示系の値を求
めた。 ・加熱発生HBr量:電気炉に加熱管をセットし、さら
に吹き込み管を備えたガス吸収瓶(蒸留水100ml)に
接続した。加熱管には試料3gを入れ、窒素ガス(約5
0ml/分)を通して電気炉で200℃で1時間加熱し
た。ガス吸収水中の臭素含量はボルハード法により定量
分析した。
-Bromine content: measured by a method according to JIS K 7299 (flask combustion method). TG (thermogravimetric analysis): Measurement was performed from room temperature to 700 ° C. at a rate of 10 ° C./min in an air atmosphere using a differential calorimeter (manufactured by Rigaku).・ Appearance hue: Colorimeter (CR-1 made by Minolta Camera)
00 type), and the values of L, a, and b display systems were determined. Amount of HBr generated by heating: A heating tube was set in an electric furnace, and further connected to a gas absorbing bottle (100 ml of distilled water) equipped with a blowing tube. 3 g of a sample is placed in a heating tube, and nitrogen gas (about 5
(0 ml / min) in an electric furnace at 200 ° C. for 1 hour. The bromine content in the gas-absorbed water was quantitatively analyzed by the Volhard method.

【0016】実施例2 実施例1において、三酸化二アンチモンの代わりに五酸
化二アンチモンを使用した以外は、同様の方法で臭素
化、後処理を行い、臭素化ポリスチレンの粉体215g
を得た。得られた粉体の分析結果を表1に示す。
Example 2 Bromination and post-treatment were carried out in the same manner as in Example 1 except that diantimony pentoxide was used instead of diantimony trioxide to obtain 215 g of brominated polystyrene powder.
I got Table 1 shows the analysis results of the obtained powder.

【0017】実施例3 実施例1において、ポリスチレンの代わりに緩衝材用発
泡ポリスチレン(旭化成製 アスパック サラサラ)を
用いた以外は、同様の方法で臭素化、後処理を行い、臭
素化ポリスチレンの粉体224gを得た。得られた粉体
の分析結果を表1に示す。
Example 3 A brominated polystyrene powder was prepared in the same manner as in Example 1 except that foamed polystyrene for cushioning material (Aspac Kasara Asahi Kasei) was used instead of polystyrene. 224 g were obtained. Table 1 shows the analysis results of the obtained powder.

【0018】実施例4 実施例1において、エチレンジクロリド750gの代わ
りにエチレンジクロリド750g及び水7.5gを用い
た以外は、実施例1と同様な方法で臭素化、後処理を行
い、臭素化ポリスチレンの粉体206gを得た。得られ
た粉体の分析結果を表1に示す。
Example 4 Bromination and post-treatment were carried out in the same manner as in Example 1 except that 750 g of ethylene dichloride and 7.5 g of water were used instead of 750 g of ethylene dichloride. 206 g of powder was obtained. Table 1 shows the analysis results of the obtained powder.

【0019】比較例1 実施例1において、三酸化二アンチモンを使用せずに、
実施例1と同様な方法で臭素化、後処理を行い、臭素化
ポリスチレンの粉体136gを得た。得られた粉体の分
析結果を表1に示す。
Comparative Example 1 In Example 1, without using diantimony trioxide,
Bromination and post-treatment were carried out in the same manner as in Example 1 to obtain 136 g of brominated polystyrene powder. Table 1 shows the analysis results of the obtained powder.

【0020】比較例2 実施例1において、三酸化二アンチモンの代わりに三塩
化アンチモンを使用し、エチレンジクロリド750gの
代わりにエチレンジクロリド750g及び水7.5gを
用いた以外は、実施例1と同様な方法で臭素化、後処理
を行い、臭素化ポリスチレンの粉体148gを得た。得
られた粉体の分析結果を表1に示す。
Comparative Example 2 In the same manner as in Example 1, except that antimony trichloride was used instead of diantimony trioxide, and 750 g of ethylene dichloride and 7.5 g of water were used instead of 750 g of ethylene dichloride. Bromination and post-treatment were carried out by a suitable method to obtain 148 g of brominated polystyrene powder. Table 1 shows the analysis results of the obtained powder.

【0021】比較例3 実施例1において、三酸化二アンチモンの代わりに無水
塩化アルミニウムを使用し、エチレンジクロリドの代わ
りにエチレンジクロリド750g及び水7.5gを用い
た以外は、実施例1と同様な方法で臭素化、後処理を行
い、臭素化ポリスチレンの粉体146gを得た。得られ
た粉体の分析結果を表1に示す。
Comparative Example 3 Example 1 was repeated except that anhydrous aluminum chloride was used in place of diantimony trioxide and 750 g of ethylene dichloride and 7.5 g of water were used in place of ethylene dichloride. Bromination and post-treatment were carried out by the method to obtain 146 g of brominated polystyrene powder. Table 1 shows the analysis results of the obtained powder.

【0022】[0022]

【表1】 [Table 1]

【0023】実施例1〜4で得られた臭素化ポリスチレ
ンを、強化PET樹脂及びナイロン66樹脂に配合し、
混練・ペレット化、ペレット乾燥、射出成形後に得られ
た成形品は、外観、難燃性、機械強度が優れたものであ
った。
The brominated polystyrene obtained in Examples 1 to 4 was blended with a reinforced PET resin and a nylon 66 resin,
The molded product obtained after kneading / pelletizing, pellet drying, and injection molding had excellent appearance, flame retardancy, and mechanical strength.

【0024】[0024]

【発明の効果】本発明の臭素化ポリスチレンの製造方法
は、工業化が容易で経済性にも優れている。また、本発
明の方法で得られた臭素化ポリスチレンは、耐熱性、外
観色相が優れているため、合成樹脂の難燃剤として有用
である。該難燃剤を配合し得られた成型加工品は、外
観、難燃性、機械強度が優れた商品価値の高いものとな
る。
The method for producing brominated polystyrene according to the present invention is easy to industrialize and excellent in economic efficiency. Further, the brominated polystyrene obtained by the method of the present invention is useful as a flame retardant for a synthetic resin because of its excellent heat resistance and appearance hue. The molded product obtained by blending the flame retardant is excellent in appearance, flame retardancy and mechanical strength, and has high commercial value.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平2−215807(JP,A) 特開 平1−149740(JP,A) ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-2-215807 (JP, A) JP-A-1-149740 (JP, A)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ハロゲン化炭化水素系溶媒に溶解又は分
散させたポリスチレンを、酸化アンチモン触媒の存在下
に塩化臭素と反応させることを特徴とする臭素化ポリス
チレンの製造方法。
1. A process for producing brominated polystyrene, comprising reacting polystyrene dissolved or dispersed in a halogenated hydrocarbon solvent with bromine chloride in the presence of an antimony oxide catalyst.
JP6086619A 1994-04-25 1994-04-25 Method for producing brominated polystyrene Expired - Fee Related JP2740455B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6086619A JP2740455B2 (en) 1994-04-25 1994-04-25 Method for producing brominated polystyrene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6086619A JP2740455B2 (en) 1994-04-25 1994-04-25 Method for producing brominated polystyrene

Publications (2)

Publication Number Publication Date
JPH07292026A JPH07292026A (en) 1995-11-07
JP2740455B2 true JP2740455B2 (en) 1998-04-15

Family

ID=13892046

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US6133381A (en) * 1996-09-26 2000-10-17 Albelmarle Corporation Brominated polystyrenic flame retardants
CN103370370A (en) * 2011-02-17 2013-10-23 玛耐科股份有限公司 High fluidity brominated polystyrene composition and method of producing same

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