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JPH0372567B2 - - Google Patents
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JPH0372567B2 - - Google Patents

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Publication number
JPH0372567B2
JPH0372567B2 JP58067054A JP6705483A JPH0372567B2 JP H0372567 B2 JPH0372567 B2 JP H0372567B2 JP 58067054 A JP58067054 A JP 58067054A JP 6705483 A JP6705483 A JP 6705483A JP H0372567 B2 JPH0372567 B2 JP H0372567B2
Authority
JP
Japan
Prior art keywords
red phosphorus
titanium oxide
weight
polymerization
polymer
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 - Lifetime
Application number
JP58067054A
Other languages
Japanese (ja)
Other versions
JPS59195512A (en
Inventor
Sadao Suganuma
Tatsuaki Nishimura
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.)
Nippon Chemical Industrial Co Ltd
Original Assignee
Nippon Chemical Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Chemical Industrial Co Ltd filed Critical Nippon Chemical Industrial Co Ltd
Priority to JP58067054A priority Critical patent/JPS59195512A/en
Publication of JPS59195512A publication Critical patent/JPS59195512A/en
Publication of JPH0372567B2 publication Critical patent/JPH0372567B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は酸化チタンとポリマーで被覆した改質
赤リンに関する。更に詳述すれば、発火点が高
く、ホスフインの発生量が少なく、基材となる物
質の物性を低下させない等の条件を満足すべく安
定化し、同時に赤リン固有の暗赤色を隠ぺい消色
した、特に難燃化剤として価値ある、酸化チタン
とポリマーで被覆された改質赤リンに関する。 赤リンは、樹脂の難燃化剤としてリンの含量が
高く、少量の添加で効果的な難燃性を発揮するこ
とはすでに知られている。しかも、赤リンはハロ
ゲン系難燃化剤のように有毒ガスの発生が少な
く、また固形物であるので樹脂に対して物性変化
を起こすことがなく、単なる増量剤といつた観点
から添加することができることから最近特に注目
される難燃化剤の一つである。 そして赤リンを難燃化剤として使用する際には
取扱い、貯蔵時、樹脂との混練時の発火の危険
性、有害なホスフインガスの発生、あるいは酸化
または加水分解されて生じる酸性物質による樹脂
の物理的性質、電気的性質の劣化等の問題がある
ことから従来より種々の赤リンの安定化方法が検
討されてきた。例えば、赤リンを水酸化アルミニ
ウム、水酸化マグネシウム等の無機物で処理する
方法、並びにパラフイン、ワツクス、カプロラク
タム、熱可塑性樹脂、熱硬化性樹脂等の有機質で
処理する方法等(アメリカ特許第2635953号、特
公昭45−37125、特公昭49−16354、特公昭53−
38171、特公昭54−39200)が知られている。 しかし、赤リン単独、あるいは上記方法により
安定化された赤リンはいずれも固有の濃い暗赤色
を呈するため、樹脂の難燃化剤として使用する場
合添加量がある程度以上になると、樹脂を不適当
な色彩に着色するために、色調を問題とする樹脂
部材への使用は制限されている。 そして樹脂のより自由な着色を可能にする、赤
リン固有の濃い暗赤色を隠ぺい、消色された赤リ
ン難燃化剤が期待されている現状である。 本発明者等は上記に鑑み、難燃剤として優れて
いると共に赤リン固有の暗赤色を隠ぺい消色、安
定化した改質赤リンについて研究を行つた結果、
赤リンを酸化チタンとポリマーで被覆することに
より上記目的を達成することができることを見出
し本発明を完成した。 即ち、本発明は、少なくとも、酸化チタン及び
有機ポリマーが粒子表面に被覆されてなる改質赤
リンにおいて、有機ポリマーが分子内に二重結合
を有し且つラジカル重合し得るモノマー及び重合
開始剤を用いて重合させたものであることを特徴
とする改質赤リンである。 本発明において、被覆前の赤リン(以下「赤リ
ン」と言い「改質赤リン」と区別する)は製造後
未処理のものは勿論、酸化アルミニウム、酸化マ
グネシウム等で安定化した赤リン又は黒リン等の
黄リン以外のリン同素体の混合したもの等でも差
支えなく、又通常、粒径が0.1〜100μの範囲に入
るものを用いると得られた酸化チタンとポリマー
で被覆した改質赤リンを樹脂に混入するのに樹脂
との混練性が良く好ましい。 本発明に用いる酸化チタンはルチル型およびア
ナタース型ともに用いられるが、その隠蔽度の点
からルチル型が好ましい。又、その粒径は0.01〜
1μの範囲に入るものが一般に使用されるが特に
限定はない。 酸化チタンの赤リンへの被覆量は必要とする隠
蔽度が得られるならば特に限定するものではない
が、通常は赤リン100重量部に対して30〜150重量
部である。 本発明に用いる有機ポリマーは、分子内に二重
結合を有し且つラジカル重合に得るモノマー(以
下「ラジカル重合し得るモノマー」)及び重合開
始剤を重合して得られるものが用いられる。ここ
で、使用可能なモノマーとしてはラジカル重合し
うるモノマーならば特に限定するものではない
が、具体的には例えばメタクリル酸メチル、メタ
クリル酸エチル等のメタクリル酸エステル類、ア
クリル酸メチル、アクリル酸エチル等のアクリル
酸エステル類、メタクリル酸、アクリル酸、スチ
レン、酢酸ビニル、アクリロニトリル等から選ば
れた1種又は2種以上を挙げることができる。こ
れらのモノマーを単独重合あるいは2種以上のモ
ノマーを共重合に用いる。また、改質赤リンを不
飽和ポリエステルの難燃化剤に使用する際、その
被覆がスチレン等に対して耐薬品性を要求される
等のような場合、架橋剤を共重合させることによ
り、架橋構造を有するポリマー被覆とすることも
できる。ここでいう架橋剤は、1分子中に2個以
上の重合性二重結合を有する多官能性モノマーで
あり、例えば、ジメタクリル酸エチレン、ジメタ
クリル酸ジエチレングリコール、ジメタクリル酸
テトラエチレングリコール、ジメタクリル酸1,
3−ブチレン、トリメタクリル酸トリメチロール
プロパン等がある。 この架橋剤の被覆に用いるモノマーに対する適
度な添加量はモノマー100重量部に対して1〜20
重量部である。添加量が1重量部未満であると生
成ポリマーは耐薬品性の効果に劣り、また20重量
部を越えると生成ポリマーの収率が低くなる。 重合開始剤については、過酸化ベンゾイル、過
流酸カリウム、過流酸アンモニウム、過酸化水素
等の有機あるいは無機の過酸化物系開始剤、アゾ
ビスイソブチロニトリル、2・2′−アゾビス−
(2−アミジノプロパン)二塩酸塩等のアゾ化合
物系開始剤、および亜硫酸水、亜硫酸水素ナトリ
ウム、亜硫酸アンモニウム、二酸化イオウガス等
の亜硫酸水素イオン生成化合物系開始剤などのう
ち、一種又は二種以上併用して用いる。 有機ポリマーの赤リンへの被覆量は、赤リン
100重量部に対し、5〜100重量部である。被覆量
が5重量部未満であると、赤リン粒子表面上に電
気的凝集沈着した酸化チタンの固定、赤リンの安
定化といつた面から充分な被覆効果が得られな
い。又、100重量部を越えると有機ポリマーがバ
インダーとなつて赤リンを著しく凝集させ粒度を
粗くすることがあり好ましくない。 本発明では以上の原料を用いて酸化チタンポリ
マー被覆赤リンを製造するのであるが、その際の
1つの実施態様につき述べれば、所定量の赤リ
ン、酸化チタンを水中に充分懸濁させ、PH2〜6
の懸濁液を調整し、これに上記のラジカル重合し
得るモノマー、重合開始剤、又場合によつては架
橋剤を加え重合させる。かかる赤リンの水懸濁液
濃度としては、水100重量部に対して赤リン5〜
80重量部懸濁させたものが作業性が良好である。
つまり上記濃度範囲の懸濁液が分散性が良く、赤
リンの粒子表面に均一に酸化チタンとポリマーを
被覆することができる。5重量部未満では目的物
の歩留りが悪く経済性に劣り、80重量部を越える
ときには生成ポリマーがバインダーとなり、赤リ
ン粒子間の凝集が激しく越こり、好ましくない。
通常このような水懸濁液中では赤リン粒子は負に
帯電しているものである。 ここで懸濁液のPHを2〜6の範囲に調整する
と、赤リン粒子の表面が負に帯電し、一方酸化チ
タン粒子の表面は正に帯電するために両者は電気
的に吸引すると共にモノマーの重合反応が行わ
れ、効率よく赤リンを酸化チタン及び有機モノマ
ーで強固に被覆することができる。例えば赤リン
として水酸化マグネシウムで安定化した赤リンを
採用した場合の赤リンと酸化チタンの水懸濁液の
ようにPHが6より高い条件では、酸化チタンが負
に荷電、あるいは等電点となることが多く、赤リ
ン粒子表面に凝集沈着せずに赤リンと酸化チタン
及び生成ポリマーの一体化が不完全、ポリマー収
率も低い等、問題がある。そこで液性がPH6より
高いときには、塩酸・硫酸・リン酸等の通常の鉱
酸等でPHを2〜6に調整して反応を行なう。これ
に反して安定化していない未処理赤リンの場合は
赤リン粒子表面はやや酸性を有していることが多
く、その水懸濁液は上記PH範囲内に入るのでその
まま重合反応に用いられる。酸化チタンの添加量
は特に限定はないが、通常赤リン100重量部に対
して30〜150重量部添加すれば必要とする隠蔽度
が得られる。 又、ラジカル重合し得るモノマーの添加量は赤
リン100重量部に対し、5〜100重量部である。添
加量が5重量部未満であると、赤リン粒子表面上
に電気的凝集沈着した酸化チタンの固定、赤リン
の安定化といつた面から充分な被覆効果が得られ
ない。また100重量部を越えて多量に用いると水
媒質中においての重合もかなり起こり、赤リン粒
子表面上に凝集沈着しないポリマーが多量に生成
したり、あるいは生成ポリマーがバインダーとな
つて赤リンを著しく凝集させ粒度を粗くすること
があり好ましくない。また、このようなフリーの
ポリマーが混在することは改質赤リンを樹脂と混
練する際に不必要に樹脂を汚染し、粒度が粗いこ
とは樹脂への分散性を損うことにもなる。 原料の添加順序については、赤リンと酸化チタ
ンの水懸濁液を必要に応じてPH調整した後、撹拌
しながらラジカル重合しうるモノマー、重合開始
剤等を添加し重合反応を行なうのが有利である。
しかしながら、必ずしも上記の順序で行なう必要
はなく、例えば赤リンの水懸濁液にラジカル重合
し得るモノマー、重合開始剤等を添加して重合を
開始し、重合半ばで酸化チタンを添加し、必要に
応じてPHを調整し重合を完了させる方法、あるい
は酸化チタンの水懸濁液にラジカル重合し得るモ
ノマー、重合開始剤等を添加して重合を開始し、
重合半ばで赤リンを添加し必要に応じてPHを調整
し重合を完了させる方法等も可能である。 重合反応は好ましくは窒素ガスの如き不活性ガ
ス雰囲気下で30〜90℃の加温下1〜7時間も重合
させれば充分である。重合反応終了後は常法に従
い、濾過・水洗を充分に行い乾燥する。 かくして得られた本発明の改質赤リンは赤リン
固有の濃い暗赤色を隠ぺい消色、かつ安定化でき
る。赤リンあるいは酸化チタン各々が単独で凝集
することなく赤リンが酸化チタンとポリマーで均
一に被覆されている状態は電子顕微鏡写真でも確
認され、また後述する試験例でも明らかな如く、
白度が高く、樹脂のより自由な着色を可能にす
る、発火点が高い、ホスフイン発生量が少ないと
いつた、難燃化剤として優れた酸化チタンとポリ
マー被覆赤リンが得られる。 以下、実施例・比較例・参考例・試験例を挙げ
て本発明を具体的に説明する。 実施例 1 撹拌機、温度計、還流用冷却器そして窒素ガス
導入管を備付したガラス製の200mlの反応容器に
水100mlと安定化していない未処理赤リン15.0g
を仕込み、撹拌し赤リンを水に分散させる。次い
で撹拌を続けながらAlの含水酸化物処理をした
ルチル型酸化チタン(石原産業株式会社製・商品
名タイペーク R−630)13.0gを添加して赤リ
ンに凝集沈着させる。このときの懸濁液のPHは3
であつた。さらに撹拌しながら、メタクリル酸メ
チル10.0gに架橋剤としてジメタクリル酸トリエ
チレングリコール0.3gを溶解させたモノマー液
を添加し、赤リン酸化チタン凝集粒子との接触を
十分に行なつた。その後この懸濁液の温度を60〜
65℃に調整し、重合開始剤として2・2′アゾビス
(2−アミジノプロパン)二塩酸塩を0.1g(1重
量%水溶液として10ml)を添加し窒素雰囲気中に
て2時間重合反応させた。反応終了後、冷却しこ
の懸濁液を吸引濾過、水洗をよく行ない、その濾
滓を60〜70℃で恒量となるまで減圧乾燥し、酸化
チタン及びポリマーで被覆され、外観が淡い灰白
色の改質赤リン36.8gが得られた。 実施例 2 実施例1と同様な装置及び操作で、水100ml、
未処理赤リン25.0g、主成分をAlの含水酸化物と
する処理をしたルチル型酸化チタン(石原産業株
式会社製、商品名タイペークR−820)17.5g、
を添加した。このときのPHは3であつた。次いで
酢酸ビニル10.0g、重合開始剤として過硫酸カリ
ウム0.4g(1重量%水溶液として40ml)順次添
加後、重合反応させ、赤リン固有の濃い暗赤色が
隠ぺい消色された灰白色の酸化チタンとポリマー
で被覆された改質赤リン49.3gを得た。 実施例 3 実施例1と同様な装置及び操作で、水100ml、
未処理赤リン25.0g、酸化チタン(実施例1に同
じ)15.0gを添加した。このときのPHは3であつ
た。次いでメタクリル酸メチル10.0gにスチレン
3.0gを溶解したモノマー液、重合開始剤として
硫酸水素ナトリウム2.0g(5重量%水溶液とし
て40ml)を順次添加後、重合反応させ、淡い灰白
色の酸化チタンとポリマーで被覆された改質赤リ
ン49.4gを得た。 参考例 各実施例あるいは比較例で原料として用いた赤
リン、酸化チタンの水中での各PHにおける電荷
(+または−で表示)とゼーター電位(mV)の
測定結果を第1表に示した。尚、HCl、NaOHを
用いてPH調整を行つた。
The present invention relates to modified red phosphorus coated with titanium oxide and polymer. More specifically, it has been stabilized to satisfy conditions such as a high ignition point, a small amount of phosphine generation, and no deterioration of the physical properties of the base material, and at the same time it has been decolored by concealing the dark red characteristic of red phosphorus. , relating to modified red phosphorus coated with titanium oxide and polymers, which is particularly valuable as a flame retardant. It is already known that red phosphorus has a high phosphorus content as a flame retardant for resins, and exhibits effective flame retardancy even when added in small amounts. Moreover, unlike halogen flame retardants, red phosphorus does not generate as much toxic gas, and since it is a solid substance, it does not change the physical properties of the resin, so it can be added from the perspective of being a mere filler. It is one of the flame retardants that has received particular attention recently because of its ability to When using red phosphorus as a flame retardant, there are risks of ignition during handling, storage, and kneading with resin, generation of harmful phosphine gas, or physical properties of resin due to acidic substances generated by oxidation or hydrolysis. Since there are problems such as deterioration of physical and electrical properties, various methods of stabilizing red phosphorus have been studied. For example, there are methods of treating red phosphorus with inorganic substances such as aluminum hydroxide and magnesium hydroxide, and methods of treating red phosphorus with organic substances such as paraffin, wax, caprolactam, thermoplastic resins, and thermosetting resins (US Pat. No. 2,635,953, Special Publication 1971-37125, Special Publication 49-16354, Special Publication 1973-
38171, Special Publication Showa 54-39200) is known. However, red phosphorus alone or red phosphorus stabilized by the above method exhibits a unique deep dark red color, so when used as a flame retardant for resins, if the amount added exceeds a certain level, the resin may become unsuitable. Because it is colored in a unique color, its use in resin parts where color tone is an issue is restricted. Currently, there are high expectations for a red phosphorus flame retardant that hides the deep dark red color inherent in red phosphorus and allows for more flexible coloring of resins. In view of the above, the present inventors conducted research on modified red phosphorus, which is excellent as a flame retardant and which hides, decolorizes, and stabilizes the dark red color inherent in red phosphorus.
The present invention was completed by discovering that the above object can be achieved by coating red phosphorus with titanium oxide and a polymer. That is, the present invention provides modified red phosphorus in which the particle surface is coated with at least titanium oxide and an organic polymer, in which the organic polymer has a double bond in the molecule and contains a monomer capable of radical polymerization and a polymerization initiator. It is a modified red phosphorus characterized by being polymerized using In the present invention, the red phosphorus before coating (hereinafter referred to as "red phosphorus" to distinguish from "modified red phosphorus") may be of course untreated after production, or red phosphorus stabilized with aluminum oxide, magnesium oxide, etc. A mixture of phosphorus allotropes other than yellow phosphorus, such as black phosphorus, may be used, and modified red phosphorus coated with titanium oxide and polymer obtained by using particles with a particle size in the range of 0.1 to 100μ can be used. It is preferable to mix it into a resin because it has good kneadability with the resin. Both rutile and anatase types of titanium oxide can be used in the present invention, but the rutile type is preferred from the viewpoint of its hiding degree. In addition, the particle size is 0.01~
A material within the range of 1μ is generally used, but there is no particular limitation. The amount of titanium oxide coated on red phosphorus is not particularly limited as long as the required degree of hiding can be obtained, but it is usually 30 to 150 parts by weight per 100 parts by weight of red phosphorus. The organic polymer used in the present invention is one that has a double bond in its molecule and is obtained by polymerizing a monomer obtained by radical polymerization (hereinafter referred to as a "radically polymerizable monomer") and a polymerization initiator. Here, the monomers that can be used are not particularly limited as long as they can undergo radical polymerization, but specific examples include methacrylic acid esters such as methyl methacrylate and ethyl methacrylate, methyl acrylate, and ethyl acrylate. Examples include one or more selected from acrylic esters such as methacrylic acid, acrylic acid, styrene, vinyl acetate, acrylonitrile, and the like. These monomers are used for homopolymerization or two or more types of monomers are used for copolymerization. In addition, when using modified red phosphorus as a flame retardant for unsaturated polyester, if the coating is required to have chemical resistance against styrene, etc., by copolymerizing a crosslinking agent, It is also possible to provide a polymer coating with a crosslinked structure. The crosslinking agent referred to here is a polyfunctional monomer having two or more polymerizable double bonds in one molecule, such as ethylene dimethacrylate, diethylene glycol dimethacrylate, tetraethylene glycol dimethacrylate, dimethacrylate, etc. acid 1,
Examples include 3-butylene and trimethylolpropane trimethacrylate. The appropriate amount of this crosslinking agent added to the monomer used for coating is 1 to 20 parts by weight per 100 parts by weight of the monomer.
Parts by weight. If the amount added is less than 1 part by weight, the resulting polymer will have poor chemical resistance, and if it exceeds 20 parts by weight, the yield of the resulting polymer will be low. Regarding polymerization initiators, benzoyl peroxide, potassium persulfate, ammonium persulfate, organic or inorganic peroxide initiators such as hydrogen peroxide, azobisisobutyronitrile, 2,2'-azobis-
(2-amidinopropane) dihydrochloride and other azo compound-based initiators, and hydrogen sulfite ion-forming compound initiators such as sulfite water, sodium bisulfite, ammonium sulfite, sulfur dioxide gas, etc., or a combination of two or more thereof. and use it. The amount of organic polymer covering red phosphorus is
The amount is 5 to 100 parts by weight per 100 parts by weight. If the coating amount is less than 5 parts by weight, a sufficient coating effect cannot be obtained in terms of fixation of titanium oxide electrically coagulated and deposited on the surface of red phosphorus particles and stabilization of red phosphorus. Moreover, if the amount exceeds 100 parts by weight, the organic polymer may act as a binder, causing significant agglomeration of red phosphorus and coarsening the particle size, which is not preferable. In the present invention, titanium oxide polymer-coated red phosphorus is produced using the above-mentioned raw materials.In one embodiment, a predetermined amount of red phosphorus and titanium oxide are sufficiently suspended in water, and the PH2 ~6
A suspension is prepared, and the above-mentioned radically polymerizable monomer, polymerization initiator, and optionally a crosslinking agent are added thereto and polymerized. The concentration of such an aqueous suspension of red phosphorus is 5 to 5 parts by weight of red phosphorus per 100 parts by weight of water.
A suspension of 80 parts by weight has good workability.
In other words, the suspension having the above concentration range has good dispersibility, and the surfaces of the red phosphorus particles can be uniformly coated with titanium oxide and polymer. If it is less than 5 parts by weight, the yield of the target product is poor and economical efficiency is poor, and if it exceeds 80 parts by weight, the resulting polymer becomes a binder and the agglomeration between red phosphorus particles becomes severe, which is not preferable.
Red phosphorus particles are normally negatively charged in such an aqueous suspension. When the pH of the suspension is adjusted to a range of 2 to 6, the surface of the red phosphorus particles becomes negatively charged, while the surface of the titanium oxide particles becomes positively charged, so that both electrically attract each other and the monomer The polymerization reaction is carried out, and red phosphorus can be efficiently and firmly coated with titanium oxide and organic monomer. For example, when red phosphorus stabilized with magnesium hydroxide is used as red phosphorus, when the pH is higher than 6, such as in an aqueous suspension of red phosphorus and titanium oxide, titanium oxide becomes negatively charged or has an isoelectric point. This often results in problems such as incomplete integration of red phosphorus, titanium oxide, and the resulting polymer without agglomeration and deposition on the surface of red phosphorus particles, and low polymer yield. Therefore, when the pH of the liquid is higher than 6, the reaction is carried out by adjusting the pH to 2 to 6 with ordinary mineral acids such as hydrochloric acid, sulfuric acid, or phosphoric acid. On the other hand, in the case of untreated red phosphorus that has not been stabilized, the surface of the red phosphorus particles is often slightly acidic, and its aqueous suspension falls within the above pH range, so it can be used as is in the polymerization reaction. . The amount of titanium oxide added is not particularly limited, but the required degree of hiding can usually be obtained by adding 30 to 150 parts by weight per 100 parts by weight of red phosphorus. The amount of the radically polymerizable monomer added is 5 to 100 parts by weight per 100 parts by weight of red phosphorus. If the amount added is less than 5 parts by weight, a sufficient coating effect cannot be obtained in terms of fixation of titanium oxide electrically coagulated and deposited on the surface of red phosphorus particles and stabilization of red phosphorus. In addition, if it is used in a large amount exceeding 100 parts by weight, polymerization in the aqueous medium will occur considerably, resulting in the formation of a large amount of polymer that does not coagulate on the surface of the red phosphorus particles, or the formed polymer may act as a binder, causing red phosphorus to be significantly degraded. This is not preferable as it may aggregate and coarsen the particle size. Furthermore, the presence of such free polymers unnecessarily contaminates the resin when the modified red phosphorus is kneaded with the resin, and the coarse particle size also impairs the dispersibility in the resin. Regarding the order of addition of raw materials, it is advantageous to adjust the pH of the aqueous suspension of red phosphorus and titanium oxide as necessary, and then add monomers capable of radical polymerization, polymerization initiators, etc. while stirring to perform the polymerization reaction. It is.
However, it is not always necessary to carry out the procedure in the above order; for example, start polymerization by adding a monomer capable of radical polymerization, a polymerization initiator, etc. to an aqueous suspension of red phosphorus, add titanium oxide halfway through the polymerization, and then add titanium oxide as needed. The method is to adjust the pH depending on the situation and complete the polymerization, or to start the polymerization by adding a monomer capable of radical polymerization, a polymerization initiator, etc. to an aqueous suspension of titanium oxide.
It is also possible to add red phosphorus in the middle of polymerization, adjust the pH as necessary, and complete the polymerization. The polymerization reaction is preferably carried out under an inert gas atmosphere such as nitrogen gas at a temperature of 30 DEG to 90 DEG C. for 1 to 7 hours. After the polymerization reaction is completed, the product is thoroughly filtered, washed with water, and dried according to a conventional method. The thus obtained modified red phosphorus of the present invention can hide, decolorize, and stabilize the deep dark red color inherent in red phosphorus. The state in which red phosphorus or titanium oxide did not aggregate alone and red phosphorus was uniformly coated with titanium oxide and polymer was confirmed by electron micrographs, and as is clear from the test examples described below.
Titanium oxide and polymer-coated red phosphorus are excellent as flame retardants, with high whiteness, enabling more free coloring of resin, high ignition point, and low amount of phosphine generation. Hereinafter, the present invention will be specifically explained with reference to Examples, Comparative Examples, Reference Examples, and Test Examples. Example 1 In a 200 ml glass reaction vessel equipped with a stirrer, a thermometer, a reflux condenser, and a nitrogen gas inlet tube, 100 ml of water and 15.0 g of unstabilized untreated red phosphorus were added.
and stir to disperse the red phosphorus in the water. Next, while stirring continuously, 13.0 g of rutile titanium oxide treated with a hydrous oxide of Al (manufactured by Ishihara Sangyo Co., Ltd., trade name: TYPEQ R-630) is added to coagulate and deposit on the red phosphorus. The pH of the suspension at this time is 3
It was hot. Further, while stirring, a monomer solution prepared by dissolving 0.3 g of triethylene glycol dimethacrylate as a crosslinking agent in 10.0 g of methyl methacrylate was added to ensure sufficient contact with the red titanium phosphate aggregate particles. Then the temperature of this suspension is 60~
The temperature was adjusted to 65°C, and 0.1 g (10 ml as a 1% by weight aqueous solution) of 2,2'azobis(2-amidinopropane) dihydrochloride was added as a polymerization initiator, followed by a polymerization reaction for 2 hours in a nitrogen atmosphere. After the reaction is completed, the suspension is cooled, filtered with suction, washed thoroughly with water, and the filter cake is dried under reduced pressure at 60 to 70°C until it reaches a constant weight. 36.8 g of quality red phosphorus was obtained. Example 2 Using the same equipment and operation as in Example 1, 100 ml of water,
25.0 g of untreated red phosphorus, 17.5 g of rutile-type titanium oxide (manufactured by Ishihara Sangyo Co., Ltd., trade name: TYPEQ R-820) treated to make the main component a hydrous oxide of Al,
was added. The pH at this time was 3. Next, 10.0 g of vinyl acetate and 0.4 g of potassium persulfate as a polymerization initiator (40 ml as a 1% by weight aqueous solution) were sequentially added, and a polymerization reaction was carried out to hide and erase the deep dark red characteristic of red phosphorus, producing grayish-white titanium oxide and polymer. 49.3 g of modified red phosphorus coated with Example 3 Using the same equipment and operation as in Example 1, 100 ml of water,
25.0 g of untreated red phosphorus and 15.0 g of titanium oxide (same as in Example 1) were added. The pH at this time was 3. Next, add styrene to 10.0g of methyl methacrylate.
After sequentially adding 3.0 g of monomer solution and 2.0 g of sodium hydrogen sulfate (40 ml as a 5% by weight aqueous solution) as a polymerization initiator, a polymerization reaction was carried out to produce modified red phosphorus coated with pale gray-white titanium oxide and polymer. I got g. Reference Example Table 1 shows the measurement results of the charge (indicated by + or -) and zeta potential (mV) at each PH of red phosphorus and titanium oxide used as raw materials in each Example or Comparative Example in water. In addition, PH was adjusted using HCl and NaOH.

【表】 数値のないものは懸濁液が凝集して定量的
測定が不可能であつた。
試験例 次に各実施例についてその白色度を光電白度計
(ケツト科学研究所C−1型)で測定、発火点及
びホスフイン発生量を後記の各測定法により測定
し、比較例とともに第2表に示した。
[Table] Items without numerical values are due to agglomeration of the suspension and are quantitative.
It was impossible to measure.
Test Examples Next, the whiteness of each Example was measured using a photoelectric whiteness meter (Kett Science Institute Model C-1), and the ignition point and amount of phosphine generated were measured using the measurement methods described below. Shown in the table.

【表】【table】

【表】 以上のように本発明の方法にもとづいて得られ
た酸化チタンとポリマーで被覆した改質赤リン
は、発火点、ホスフイン発生量の試験結果の点か
らみても使用上安定した被覆を持つていることが
わかる。 また、本発明の実施例1で得られた改質赤リン
の電子顕微鏡写真を第1図a〜cに、比較例3で
得られた赤リンの電子顕微鏡写真を第2図a〜c
に示す。これらの写真図からも本願発明は被覆が
十分になされていることが判る。 発火点測定法 装置は外部を断熱材でおおつた底面積200cm2
さ25cmの円筒形の電気炉を用いた。底部中心より
約10cmの位置に10mlのルツボが保持できるように
なつている。 測定はルツボに3gの赤リンを入れルツボの中
心部に熱電対を差し入れ2.7℃/分の昇温速度で
温度上昇をおこなう。ある点までくると温度が急
激に上昇し発火が始まる。温度が急激に上昇する
直前の温度を発火点とした。 本実施例及び比較例における発火点は同様の測
定を3回行ないそれを平均したものである。1以
下は四捨五入とした。 ホスフイン発生量の測定法 (1) 25℃のとき 試料10gを1000mlのフラスコに入れ密閉し、
24時間25℃±0.5℃の恒温槽中に放置する。放
置後フラスコ内の気体中のホスフイン濃度を検
知管で定量し、この数値を赤リン1g当たりの
ホスフイン発生量に換算する。 (2) 80℃のとき 試料10gをあらかじめ80℃±0.5℃の油浴に
浸してある1000mlのフラスコに入れ密閉し、30
分間放置する。放置後フラスコ内の気体中のホ
スフイン濃度を検知管で定量し、この数値を赤
リン1g当たりのホスフイン発生量に換算す
る。 (3) 150℃のとき 試料1gをあらかじめ150℃±0.5℃の油浴に
浸してある1000mlのフラスコに入れ密閉し、30
分間放置する。放置後フラスコ内の気体中のホ
スフイン濃度を検知管で測定し、この数値を赤
リン1g当たりのホスフイン発生量に換算す
る。 なお値はそれぞれ3回の測定を行ない、それ
らの平均値である。
[Table] As described above, the modified red phosphorus coated with titanium oxide and polymer obtained based on the method of the present invention has a stable coating in terms of test results for ignition point and amount of phosphine generated. I know that I have it. Further, electron micrographs of the modified red phosphorus obtained in Example 1 of the present invention are shown in Figures 1 a to c, and electron micrographs of the red phosphorus obtained in Comparative Example 3 are shown in Figures 2 a to c.
Shown below. It can be seen from these photographs that the present invention is sufficiently coated. Ignition point measurement method The device used was a cylindrical electric furnace with a base area of 200 cm 2 and a height of 25 cm, the outside of which was covered with a heat insulating material. It is designed to hold a 10ml crucible at a position approximately 10cm from the center of the bottom. For measurement, 3g of red phosphorus is placed in a crucible, a thermocouple is inserted into the center of the crucible, and the temperature is raised at a rate of 2.7°C/min. Once it reaches a certain point, the temperature rises rapidly and ignition begins. The ignition point was defined as the temperature just before the temperature suddenly rose. The ignition points in this example and comparative example were determined by averaging three similar measurements. Values below 1 were rounded off. Measuring method for the amount of phosphine generated (1) At 25℃ Place 10g of sample in a 1000ml flask and seal it.
Leave it in a constant temperature bath at 25℃±0.5℃ for 24 hours. After standing, the concentration of phosphine in the gas in the flask is determined using a detection tube, and this value is converted to the amount of phosphine generated per 1 g of red phosphorus. (2) At 80℃ Place 10g of the sample in a 1000ml flask that has been immersed in an oil bath at 80℃±0.5℃, seal it, and heat it for 30 minutes.
Leave for a minute. After standing, the concentration of phosphine in the gas in the flask is determined using a detection tube, and this value is converted to the amount of phosphine generated per 1 g of red phosphorus. (3) When the temperature is 150℃ Place 1g of the sample in a 1000ml flask that has been immersed in an oil bath at 150℃±0.5℃, seal it, and heat it for 30 minutes.
Leave for a minute. After standing, the phosphine concentration in the gas in the flask is measured with a detection tube, and this value is converted to the amount of phosphine generated per 1 g of red phosphorus. Note that each value was measured three times and is the average value thereof.

【図面の簡単な説明】[Brief explanation of drawings]

第1図a〜cは本発明の実施例1で得られた改
質赤リンの電子顕微鏡写真であり、第2図a〜c
は比較例3で得られた赤リンの電子顕微鏡写真で
ある。
Figures 1 a to c are electron micrographs of modified red phosphorus obtained in Example 1 of the present invention, and Figures 2 a to c
is an electron micrograph of red phosphorus obtained in Comparative Example 3.

Claims (1)

【特許請求の範囲】[Claims] 1 少なくとも、酸化チタン及び有機ポリマーが
粒子表面に被覆されてなる改質赤リンであつて、
有機ポリマーが分子内に二重結合を有し且つラジ
カル重合し得るモノマー及び重合開始剤を用いて
重合させたものであることを特徴とする改質赤リ
ン。
1 Modified red phosphorus whose particle surfaces are coated with at least titanium oxide and an organic polymer,
A modified red phosphorus characterized in that the organic polymer has a double bond in the molecule and is polymerized using a monomer capable of radical polymerization and a polymerization initiator.
JP58067054A 1983-04-18 1983-04-18 Manufacture of modified red phosphorus Granted JPS59195512A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58067054A JPS59195512A (en) 1983-04-18 1983-04-18 Manufacture of modified red phosphorus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58067054A JPS59195512A (en) 1983-04-18 1983-04-18 Manufacture of modified red phosphorus

Publications (2)

Publication Number Publication Date
JPS59195512A JPS59195512A (en) 1984-11-06
JPH0372567B2 true JPH0372567B2 (en) 1991-11-19

Family

ID=13333735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58067054A Granted JPS59195512A (en) 1983-04-18 1983-04-18 Manufacture of modified red phosphorus

Country Status (1)

Country Link
JP (1) JPS59195512A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3905039A1 (en) * 1989-02-18 1990-08-23 Hoechst Ag PHLEGMATIZED RED PHOSPHOR
JP3935012B2 (en) 2002-07-18 2007-06-20 日本化学工業株式会社 Modified red phosphorus, process for producing the same, decolorized red phosphorus composition and flame retardant polymer composition

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5693739A (en) * 1979-12-27 1981-07-29 Showa Electric Wire & Cable Co Ltd Flame-retarding polyolefin composition

Also Published As

Publication number Publication date
JPS59195512A (en) 1984-11-06

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