JPH0428740B2 - - Google Patents
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- JPH0428740B2 JPH0428740B2 JP58012555A JP1255583A JPH0428740B2 JP H0428740 B2 JPH0428740 B2 JP H0428740B2 JP 58012555 A JP58012555 A JP 58012555A JP 1255583 A JP1255583 A JP 1255583A JP H0428740 B2 JPH0428740 B2 JP H0428740B2
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- Prior art keywords
- flame retardant
- resin
- granular
- thermoplastic resin
- parts
- Prior art date
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Description
本発明は可燃性の熱可塑性樹脂成形時に樹脂ペ
レツトへ混合して成形することにより、難燃性の
成形品を製造するための粒状難燃剤に関する。
一般に難燃性の熱可塑性樹脂成形品を得るため
には、樹脂ペレツトに難燃性を添加し成形機内で
難燃化剤を溶融した樹脂と混合して成形するのが
便利である。その場合難燃剤を粉末のまゝで使用
するとダストが生じ、作業環境に悪い。流れの悪
い粉末状または液状の難燃剤を使用すると自動連
続計量の際に効率が悪く、計量誤差を生じ易い。
また粉末状の場合は樹脂ペレツトと混合する過程
において形状の相違により分級したり、うまく展
着せず不均一混合になり易い。また混合熱によつ
て供給ホツパー内でブリツジを生じ、樹脂の連続
成形が困難になり、また成形機のスクリユーへの
くい込みが異なるので不均一混合になり易い。
そこで難燃剤と樹脂とで難燃剤30重量%のマス
ターバツチをつくり、これを樹脂ペレツトに混入
する方法や、難燃剤を適当な大きさの粒状物とし
て添加する方法が試みられたが、従来の造粒法で
は難燃剤自体を打錠法、ローラー圧縮法、スプレ
ー顆粒化法、回転式造粒法等で造粒するため、必
要な粒度が得られない、粒度が不均一になり流れ
に問題を生ずる、強度が不充分で輸送、混合過程
で崩壊する、高温長時間の混練により難燃剤が分
解する、難燃効果を上げるために上記マスターバ
ツチを多量に投入しなければならない等の欠点が
あつた。
本発明はこれらの欠点を克服するため、流動性
にすぐれ、所定の比較的均一な粒度を持ち、輸送
および混合過程において崩壊し難いが、樹脂ペレ
ツトに混合して成形機にかければ樹脂中に均一に
分散することができ、しかも多量の樹脂ペレツト
で希釈できる粒状難燃剤を提供する。
本発明によれば、難燃剤70重量%以上と、熱可
塑性樹脂30重量%以下とを含有した粒状難燃剤が
提供される。
こゝでいう難燃剤とは、常温で液体または固体
であつて、可燃性物質に添加することによつてそ
れを難燃化し得る臭素含有芳香族もしくは脂環族
ハロゲン系難燃剤化合物を意味する。これらの難
燃剤自体は公知であり、その例としては、ハロゲ
臭素を含有する化合物であり、具体例としては、
テトラブロムジフエニルエーテル、ヘキサブロム
ジフエニルエーテル、デカブロムジフエニルエー
テル、ヘキサブロムシクロドデカン、モノクロル
ペンタブロムシクロヘキサン、トリブロムフエニ
ルアリルエーテル、トリブロムフエニルメタアリ
ルエーテル、2,2−ビス(4−アリロキシ−
3,5−ジブロムフエニル)プロパン、2,2−
ビス(4−メタアリロキシ−3,5−ジブロムフ
エニル)プロパン、2,2−ビス(4−ジブロム
プロポキシ−3,5−ジブロムフエニル)プロパ
ン、2,2−ビス(4−ジブロムイソブチロキシ
−3,5−ジブロムフエニル)プロパン、ブタジ
エンまたはイソプレンまたはクロロプレンの二量
体および三量体のハロゲン化物、これらの混合物
等がある。なかでも融点150℃以上の難燃剤と融
点150℃以下の難燃剤とを重量で1対0.1〜1対1
の割合で混合したものがよく、例えばヘキサブロ
ムシクロドデカンと2,2−ビス(4−アリロキ
シ−3,5−ジブロムフエニル)プロパンおよ
び/またはトリブロムフエニルアリルエーテルと
を上記割合で混合したものが最も好ましい。これ
らは造粒機中で発熱し、、強固に固まるからであ
る。
熱可塑性樹脂としては、例えばポリスチレン樹
脂、ポリメタクリル酸メチル樹脂、スチレン−ブ
タジエン共重合体樹脂、スチレン−無水マレイン
酸共重合体樹脂、ポリエステル樹脂、ポリアミド
樹脂、ポリエチレン樹脂、エチレン−酢酸ビニル
樹脂、塩素化ポリエチレン樹脂、ポリ塩化ビニル
樹脂、ポリカーボネート樹脂等の各種の樹脂が用
いられる。なかでも、溶剤に溶け易く、乾燥し易
く、また強固にして吸湿性がなく、かつ成形機中
で容易に解粒し易い粒状難燃剤を得るためには、
スチレン、ブタジエン、アクリル酸およびその誘
導体からなる群から選ばれた単量体の重合体また
は共重合体が好ましい。
次に、造粒する難燃剤と熱可塑性樹脂との割合
は、得られる粒状難燃剤中に難燃剤が70〜99.5重
量%以上、熱可塑性樹脂が30〜0.5重量%以下と
なるような割合である。この範囲より外れると本
発明の目的とする効果が得られない。
難燃剤70〜99.5重量%以上と熱可塑性樹脂30〜
0.5重量%以下とを含む組成物を所定の大きさの
粒状物に造粒するにはいくつかの方法がある。例
えば
イ 難燃剤を熱可塑性樹脂の溶液で練合し、造粒
する方法
ロ 組成物を圧縮してシート状塊をつくり、切断
もしくは粉砕する方法
等である。
まず難燃剤を熱可塑性樹脂の溶液で練合し、練
合した塊を造粒し、溶剤を乾燥して粒状難燃剤を
得る方法について述べる。この方法に使用し得る
溶剤としては、熱可塑性樹脂を溶解するものであ
ればよく、比較的沸点の低い塩素を含有するもの
が溶解し易く、強固なものが得られ、防災、乾燥
上好ましい。例えば塩化メチレン、クロロホル
ム、トリクロルエチレン、四塩化炭素、ベンゼ
ン、トルエン、キシレン、メチルエチルケトンお
よびそれらの混合物等がある。溶液の濃度は難燃
剤を均一に練合し、造粒し得る限り省資源および
作業環境上できるだけ高濃度が好ましい。
造粒方法は難燃剤を樹脂溶液で練合した塊を一
定の粒度に成形し得る限り公知の方法を用いるこ
とができるが、なかでも押出し機を使用する方法
が粒径のそろつた強固な粒状物が生産性良く得ら
れるので好ましい。例えば二軸スクリユー型押出
し機で口金より押し出し、所定の粒径の粒状物を
得る押出し成形法が好ましい。
次に組成物を圧縮してシート状塊をつくり、切
断もしくは粉砕する方法について述べる。
この方法に使用し得る難燃剤としては、粉末ま
たは粉末で加熱溶融するものであればよく、熱可
塑性樹脂としても同様に粉末で加熱溶融するもの
であればよい。そしてこれらの難燃剤および熱可
塑性樹脂を粉末同志で混合して均一組成物とす
る。この組成物を加熱ロールまたは加熱プレスで
圧縮してシート状塊をつくり粉砕する。
造粒した難燃剤の大きさは本発明の粒状難燃剤
を使用する用途や添加する成形用樹脂ペレツトと
の大きさにもよるが、一般に直径0.5〜8mmのペ
レツト、特に直径が0.5〜5mmで長さが直径1〜
10倍であるペレツトが乾燥し易く、強固でかつ樹
脂と均一に混合できるので好ましい。
本発明の粒状難燃剤は必要に応じ樹脂改質剤、
例えば三酸化アンチモン、酸化チタン、酸化モリ
ブデン、ケイ酸ジルコニウム、ホウ酸亜鉛等の難
燃助剤、安定剤、着色剤、耐候剤、紫外線吸収
剤、つや消剤、帯電防止剤、増量剤およびその他
の配合剤を含むことができる。
本発明によれば、難燃剤70〜99.5重量%と熱可
塑性樹脂30〜0.5重量%とからなる粒状難燃剤で
あり、粒状品の計量、輸送、樹脂との混合過程に
おいて崩壊することがなく、ダストの生じる恐れ
もない。また少量の粒状難燃剤で多量の樹脂ペレ
ツトに希釈でき、混合作業が改善される。しかも
成形時樹脂に均一に分散させることができる。
以下実施例により本発明をさらに詳細に説明す
る。部および%は重量基準である。
実施例 1ないし3
難燃剤75部、30%ポリメタクリル酸メチル樹脂
(旭化成製テルペツト80N)塩化メチレン溶液10
部をハイスピードミキサー(深江工業製)に仕込
み、アジテーター400rpm、チヨツパー300rpmに
て2分間混合する。混合した配合品を二軸スクリ
ユー式連続押出し機(深江工業製、FSWG型3B
型)のホツパーに投入し、3mm径の目を有するス
クリーンにて90Kg/時の速度で連続的に押出し、
直径3mm、長さ7〜10mmの粒状品を得た。次に塩
化メチレンを除去するためこれを流動乾燥機で乾
燥し、粒状品の強度を測定した。
実施例で得た粒状品の強度を表1に示す。
The present invention relates to a granular flame retardant for producing flame-retardant molded articles by mixing it into resin pellets during molding of a flammable thermoplastic resin. Generally, in order to obtain a flame-retardant thermoplastic resin molded article, it is convenient to add flame retardant to resin pellets, mix the flame retardant with a molten resin in a molding machine, and mold the mixture. In this case, if the flame retardant is used in powder form, dust will be generated, which is bad for the working environment. If a powder or liquid flame retardant that does not flow well is used, automatic continuous metering will be inefficient and prone to metering errors.
In addition, if it is in powder form, it is likely to be classified due to differences in shape during the process of mixing with resin pellets, or it will not spread well, resulting in non-uniform mixing. In addition, bridging occurs in the supply hopper due to the heat of mixing, making continuous molding of the resin difficult, and uneven mixing is likely to occur because the screws are inserted into the screws of the molding machine differently. Therefore, attempts have been made to create a masterbatch containing 30% flame retardant by weight of flame retardant and resin and mix this into resin pellets, or to add flame retardant as granules of appropriate size, but conventional methods In the granulation method, the flame retardant itself is granulated using a tableting method, roller compression method, spray granulation method, rotary granulation method, etc., so the required particle size may not be obtained or the particle size may become uneven, causing problems with flow. There were disadvantages such as: the strength was insufficient and it collapsed during transportation and mixing; the flame retardant decomposed due to long-term kneading at high temperatures; and a large amount of the above masterbatch had to be added to increase the flame retardant effect. . In order to overcome these disadvantages, the present invention has excellent fluidity, a predetermined relatively uniform particle size, and is difficult to disintegrate during transportation and mixing processes, but when mixed with resin pellets and put into a molding machine, it can be mixed into resin pellets. To provide a granular flame retardant that can be uniformly dispersed and diluted with a large amount of resin pellets. According to the present invention, a granular flame retardant containing 70% by weight or more of a flame retardant and 30% by weight or less of a thermoplastic resin is provided. The flame retardant referred to here means a bromine-containing aromatic or alicyclic halogen flame retardant compound that is liquid or solid at room temperature and can be added to a flammable substance to make it flame retardant. . These flame retardants themselves are publicly known, and examples include compounds containing halogen bromine; specific examples include:
Tetrabrom diphenyl ether, hexabrom diphenyl ether, decabrom diphenyl ether, hexabrom cyclododecane, monochloropentabrom cyclohexane, tribrom phenyl allyl ether, tri brom phenyl metaallyl ether, 2,2-bis(4 -Allyloxy-
3,5-dibromphenyl)propane, 2,2-
Bis(4-methallyloxy-3,5-dibromophenyl)propane, 2,2-bis(4-dibromopropoxy-3,5-dibromophenyl)propane, 2,2-bis(4-dibromoisobutyroxy-3, Dimeric and trimeric halides of 5-dibromophenyl)propane, butadiene or isoprene or chloroprene, mixtures thereof, and the like. In particular, a flame retardant with a melting point of 150℃ or higher and a flame retardant with a melting point of 150℃ or lower at a ratio of 1:0.1 to 1:1 by weight.
For example, a mixture of hexabromocyclododecane and 2,2-bis(4-allyloxy-3,5-dibromphenyl)propane and/or tribromphenyl allyl ether in the above ratio is preferable. Most preferred. This is because these materials generate heat in the granulator and solidify. Examples of thermoplastic resins include polystyrene resin, polymethyl methacrylate resin, styrene-butadiene copolymer resin, styrene-maleic anhydride copolymer resin, polyester resin, polyamide resin, polyethylene resin, ethylene-vinyl acetate resin, and chlorine. Various resins such as polyethylene resin, polyvinyl chloride resin, and polycarbonate resin are used. In particular, in order to obtain a granular flame retardant that is easily soluble in solvents, easy to dry, strong, non-hygroscopic, and easily disintegrated in a molding machine,
Polymers or copolymers of monomers selected from the group consisting of styrene, butadiene, acrylic acid and derivatives thereof are preferred. Next, the ratio of the flame retardant to be granulated and the thermoplastic resin is such that the flame retardant is 70 to 99.5% by weight or more and the thermoplastic resin is 30 to 0.5% by weight or less in the resulting granular flame retardant. be. If it deviates from this range, the desired effect of the present invention cannot be obtained. Flame retardant 70~99.5% by weight or more and thermoplastic resin 30~
There are several methods for granulating a composition containing 0.5% by weight or less into granules of a predetermined size. For example, (a) a method in which a flame retardant is kneaded with a solution of a thermoplastic resin and granulated; (b) a method in which the composition is compressed to form a sheet-like mass and then cut or crushed. First, a method will be described in which a flame retardant is kneaded with a thermoplastic resin solution, the kneaded mass is granulated, and the solvent is dried to obtain a granular flame retardant. The solvent that can be used in this method may be any solvent as long as it dissolves the thermoplastic resin, and those containing chlorine, which has a relatively low boiling point, are easy to dissolve and provide a strong solvent, which is preferable in terms of disaster prevention and drying. Examples include methylene chloride, chloroform, trichloroethylene, carbon tetrachloride, benzene, toluene, xylene, methyl ethyl ketone, and mixtures thereof. The concentration of the solution is preferably as high as possible in terms of resource saving and working environment, as long as the flame retardant can be uniformly kneaded and granulated. As a granulation method, any known method can be used as long as it is possible to form a mass made by kneading flame retardant with a resin solution into a fixed particle size, but among them, a method using an extruder is used to form strong granules with uniform particle size. It is preferable because the product can be obtained with good productivity. For example, an extrusion molding method in which granules of a predetermined particle size are obtained by extruding from a die using a twin-screw extruder is preferred. Next, a method of compressing the composition to form a sheet-like mass and cutting or crushing the mass will be described. The flame retardant that can be used in this method may be a powder or one that can be heated and melted in the form of a powder, and the thermoplastic resin may be one that can be similarly heated and melted in the form of a powder. These flame retardants and thermoplastic resins are then mixed in powder form to form a homogeneous composition. This composition is compressed with a heated roll or heated press to form a sheet-like mass, which is then crushed. The size of the granulated flame retardant depends on the purpose for which the granular flame retardant of the present invention is used and the size of the molding resin pellets to be added, but it is generally pellets with a diameter of 0.5 to 8 mm, particularly pellets with a diameter of 0.5 to 5 mm. Length is 1 to diameter
Pellets with a density of 10 times are preferred because they are easy to dry, strong, and can be mixed uniformly with the resin. The granular flame retardant of the present invention may optionally contain a resin modifier,
For example, flame retardant aids such as antimony trioxide, titanium oxide, molybdenum oxide, zirconium silicate, zinc borate, stabilizers, colorants, weathering agents, ultraviolet absorbers, matting agents, antistatic agents, extenders, and others. may contain combinations of. According to the present invention, the granular flame retardant is composed of 70 to 99.5% by weight of flame retardant and 30 to 0.5% by weight of thermoplastic resin, and does not disintegrate during the process of weighing, transporting, or mixing the granular product with resin. There is no risk of dust generation. Also, a small amount of particulate flame retardant can be diluted into a large amount of resin pellets, improving mixing operations. Moreover, it can be uniformly dispersed in the resin during molding. The present invention will be explained in more detail with reference to Examples below. Parts and percentages are by weight. Examples 1 to 3 75 parts of flame retardant, 30% polymethyl methacrylate resin (Terpet 80N manufactured by Asahi Kasei) methylene chloride solution 10
Place the mixture in a high-speed mixer (manufactured by Fukae Kogyo) and mix for 2 minutes with an agitator at 400 rpm and a chopper at 300 rpm. The mixed product is extruded using a twin-screw continuous extruder (manufactured by Fukae Kogyo, FSWG type 3B).
hopper of a mold) and continuously extruded at a speed of 90 kg/hour through a screen with 3 mm diameter openings.
A granular product with a diameter of 3 mm and a length of 7 to 10 mm was obtained. This was then dried in a fluidized fluid dryer to remove methylene chloride, and the strength of the granular product was measured. Table 1 shows the strength of the granular products obtained in Examples.
【表】
実施例 4ないし6
難燃剤100部、20%ポリスチレンのトルエン溶
液20部を使用し、実施例1〜3と同様の操作によ
つて粒状品を得た。得られた粒状品の強度を表2
に示す。[Table] Examples 4 to 6 Granular products were obtained in the same manner as in Examples 1 to 3 using 100 parts of a flame retardant and 20 parts of a 20% polystyrene solution in toluene. Table 2 shows the strength of the obtained granular products.
Shown below.
【表】
実施例 7
ポリスチレン樹脂(新日本製鉄化学工業製エス
チレンG−20)2000部、粒状難燃剤70部をリボン
ブレンダーで10分間混合した。次にこれを3×6
×15mmの金型を用いて230℃で射出成形した。試
料は10シヨツト毎に1本合計10本サンプリング
し、ASTM D−2863の方法で燃焼試験を行な
い、酸素濃度指数(LOI値)のバラツキを見た。
結果を表3に示す。[Table] Example 7 2000 parts of polystyrene resin (Estyrene G-20 manufactured by Nippon Steel Chemical Industry Co., Ltd.) and 70 parts of a granular flame retardant were mixed for 10 minutes using a ribbon blender. Next, convert this to 3x6
Injection molding was performed at 230°C using a ×15 mm mold. A total of 10 samples were taken, one every 10 shots, and a combustion test was conducted using the ASTM D-2863 method to check for variations in the oxygen concentration index (LOI value).
The results are shown in Table 3.
【表】
実施例 8ないし10
難燃剤75部、三酸化アンチモン25部、30%ボリ
メタクリル酸メチル樹脂(旭化成製テルペツト
80N)塩化メチレン溶液10部を使用し、実施例1
〜3と同様の操作によつて粒状品を得た。得られ
た粒状品の強度を表4に示す。[Table] Examples 8 to 10 75 parts of flame retardant, 25 parts of antimony trioxide, 30% polymethyl methacrylate resin (Terpet, manufactured by Asahi Kasei)
Example 1 using 10 parts of 80N) methylene chloride solution
A granular product was obtained by the same operation as in 3. Table 4 shows the strength of the obtained granular product.
【表】
実施例 11ないし13
難燃剤100部、20%ポリスチレン樹脂のトルエ
ン溶液20部を使用して実施例1〜3と同様の操作
によつて粒状品を得た。得られた粒状品の強度を
表5に示す。[Table] Examples 11 to 13 Granular products were obtained in the same manner as in Examples 1 to 3 using 100 parts of a flame retardant and 20 parts of a toluene solution of 20% polystyrene resin. Table 5 shows the strength of the obtained granular products.
【表】
実施例 14
ポリプロピレン樹脂(宇部興産製J−115G)
2000部、粒状難燃剤70部をリボンブレンダーで10
分間混合した。次にこれを3×6×15mmの金型を
用いて230℃で射出成形した。試料は10シヨツト
毎に1本合計10本サンプリングし、ASTM D−
2863の方法で燃焼試験を行ない、酸素濃度指数
(LOI値)のバラツキを見た。結果を表6に示す。[Table] Example 14 Polypropylene resin (J-115G manufactured by Ube Industries)
2000 parts and 70 parts of granular flame retardant in a ribbon blender.
Mixed for a minute. Next, this was injection molded at 230°C using a 3 x 6 x 15 mm mold. A total of 10 samples were taken, one every 10 shots, and the ASTM D-
A combustion test was conducted using the 2863 method, and variations in the oxygen concentration index (LOI value) were observed. The results are shown in Table 6.
【表】
実施例 15
難燃剤90部および熱可塑性樹脂10部を粉末同志
で均一に混合した。組成物を熱プレスで150℃、
50Kg/cm2の圧力で3分間圧縮し、1mmの板状に
し、60℃に冷却して粒状品を得た。得られた粒状
品の強度を測定した。
次にポリスチレン樹脂(新日本製鉄化学製エス
チレンG−20)2000部、粒状難燃剤70部をリボン
ブレンダーで10分間混合した。次にこれを3×6
×15mmの金型を用いて230℃で射出成形した。試
料は10シヨツト毎に1本合計10本サンプリング
し、ASTM D−2863の方法で燃焼試験を行な
い、酸素濃度指数(LOI値)のバラツキを見た。
それらの結果を表7に示す。[Table] Example 15 90 parts of flame retardant and 10 parts of thermoplastic resin were uniformly mixed as powders. Heat press the composition at 150℃,
The mixture was compressed for 3 minutes at a pressure of 50 kg/cm 2 to form a 1 mm plate, and cooled to 60° C. to obtain a granular product. The strength of the obtained granules was measured. Next, 2000 parts of polystyrene resin (Estyrene G-20 manufactured by Nippon Steel Chemical Co., Ltd.) and 70 parts of a granular flame retardant were mixed for 10 minutes using a ribbon blender. Next, convert this to 3x6
Injection molding was performed at 230°C using a ×15 mm mold. A total of 10 samples were taken, one every 10 shots, and a combustion test was conducted using the ASTM D-2863 method to check for variations in the oxygen concentration index (LOI value).
The results are shown in Table 7.
Claims (1)
は脂環族ハロゲン系難燃剤化合物またはその混合
物70〜99.5重量%以上と、バインダーとして熱可
塑性樹脂30〜0.5重量%以下を含有することを特
徴とする熱可塑性樹脂成形品添加用の粒状難燃
剤。 2 前記熱可塑性樹脂バインダーがスチレン、ブ
タジエン、アクリル酸およびその誘導体からなる
群から選ばれた単量体の重合体または共重合体で
ある特許請求の範囲第1項記載の粒状難燃剤。[Scope of Claims] 1. 70 to 99.5% by weight or more of a bromine-containing aromatic or alicyclic halogen flame retardant compound or a mixture thereof for addition to a thermoplastic resin, and 30 to 0.5% by weight or less of a thermoplastic resin as a binder. A granular flame retardant for addition to thermoplastic resin molded products, characterized by containing the following. 2. The granular flame retardant according to claim 1, wherein the thermoplastic resin binder is a polymer or copolymer of monomers selected from the group consisting of styrene, butadiene, acrylic acid, and derivatives thereof.
Priority Applications (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1255583A JPS59138242A (en) | 1983-01-27 | 1983-01-27 | Granular flame-retardant |
| KR1019840000160A KR910007599B1 (en) | 1983-01-27 | 1984-01-16 | Granular organohalide flame retardant additive |
| IE107/84A IE56570B1 (en) | 1983-01-27 | 1984-01-18 | Granular organohalide flame retardant additive and methods of preparing the same |
| AU23738/84A AU569864B2 (en) | 1983-01-27 | 1984-01-24 | Granular organohalide flame retardant additive |
| CA000446059A CA1257033A (en) | 1983-01-27 | 1984-01-25 | Granular organohalide flame retardant additive |
| NO840288A NO162293C (en) | 1983-01-27 | 1984-01-25 | GRANULATED, FLAMMABLE ORGANOAL HALOGENIDE ADDITIVE AND THE PREPARATION AND USE OF THEREOF. |
| DE8484100828T DE3466546D1 (en) | 1983-01-27 | 1984-01-26 | Granular organohalide flame retardant additive and methods of preparing the same |
| EP84100828A EP0115341B1 (en) | 1983-01-27 | 1984-01-26 | Granular organohalide flame retardant additive and methods of preparing the same |
| FI840319A FI76584C (en) | 1983-01-27 | 1984-01-26 | Granular flame retardant organohalide additive composition |
| US06/574,766 US4530880A (en) | 1983-01-27 | 1984-01-27 | Granular organohalide flame retardant additive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1255583A JPS59138242A (en) | 1983-01-27 | 1983-01-27 | Granular flame-retardant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59138242A JPS59138242A (en) | 1984-08-08 |
| JPH0428740B2 true JPH0428740B2 (en) | 1992-05-15 |
Family
ID=11808582
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1255583A Granted JPS59138242A (en) | 1983-01-27 | 1983-01-27 | Granular flame-retardant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59138242A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2551175B2 (en) * | 1989-12-12 | 1996-11-06 | 東レ株式会社 | Flame-retardant polyester composition |
| JP4622040B2 (en) * | 2000-05-15 | 2011-02-02 | 東ソー株式会社 | Resin composition |
| BRPI0418907A (en) * | 2004-05-20 | 2007-11-27 | Albemarle Corp | unchanged brominated anionic styrene polymer agglomerates and preparation method |
| JP2007070586A (en) * | 2005-09-02 | 2007-03-22 | Kyodo Chem Co Ltd | Granular flame retarder composition |
| WO2010127072A1 (en) * | 2009-05-01 | 2010-11-04 | Albemarle Corporation | Pelletized low molecular weight brominated aromatic polymer compositions |
| JP5422636B2 (en) * | 2011-11-28 | 2014-02-19 | アルベマール・コーポレーシヨン | Pelletized brominated anionic styrenic polymer |
| JP6831327B2 (en) * | 2015-07-29 | 2021-02-17 | 東洋スチレン株式会社 | Flame retardant masterbatch and its manufacturing method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5613725B2 (en) * | 1972-10-02 | 1981-03-31 | ||
| JPS5095347A (en) * | 1973-12-25 | 1975-07-29 | ||
| JPS5290543A (en) * | 1976-01-23 | 1977-07-29 | Iwao Hishida | Granular compositions of waxes |
-
1983
- 1983-01-27 JP JP1255583A patent/JPS59138242A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59138242A (en) | 1984-08-08 |
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