JP4525191B2 - Pigment compositions and their use in plastics - Google Patents
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Description
本発明は、着色用の顔料組成物に関し、詳しくは、フタロシアニン系顔料を主な着色成分とする着色剤およびそれにより着色された反りや変形の少ないプラスチック成形品に関する。 The present invention relates to a pigment composition for coloring, and in particular, to a colorant containing a phthalocyanine pigment as a main coloring component and a plastic molded product colored thereby with less warpage and deformation.
プラスチック着色剤として使用されているフタロシアニン系顔料は、耐光性、耐熱性、耐移行性、鮮明な色相、高い着色力等の特性を有するが、ポリオレフィンやポリエチレンテレフタレートなどの部分的に結晶性を有する熱可塑性樹脂の着色に用いた場合、成型時において樹脂の結晶化度や結晶化方向に影響を与え、結果として、プラスチック成形品に反りや変形が生じる。この原因については、フタロシアニン系顔料が樹脂の結晶化剤として働くためと考えられている。 Phthalocyanine pigments used as plastic colorants have characteristics such as light resistance, heat resistance, migration resistance, clear hue, high coloring power, etc., but partially crystalline such as polyolefin and polyethylene terephthalate. When used for coloring a thermoplastic resin, it affects the crystallinity and crystallization direction of the resin during molding, resulting in warping and deformation of the plastic molded product. The reason for this is thought to be because the phthalocyanine pigment acts as a resin crystallization agent.
プラスチック成形品の反りや変形を改善するため、成形メーカーでは、成形温度、射出圧、射出時間、射出速度、冷却時間等の加工条件を変えることにより最適化を行っている。しかし、樹脂の種類、着色剤、添加剤及び成形品の大きさや形状により収縮率が異なる為、反りや変形を予測した加工条件の設定は困難であった。また、成形サイクルを長くし、生産性を悪くする場合が多かった。 In order to improve the warping and deformation of plastic molded products, molding manufacturers are optimizing by changing processing conditions such as molding temperature, injection pressure, injection time, injection speed, and cooling time. However, since the shrinkage varies depending on the type of resin, colorant, additive, and size and shape of the molded product, it is difficult to set processing conditions that predict warpage and deformation. Moreover, the molding cycle was lengthened and the productivity was often deteriorated.
反りや変形を改善する他の方法としては、強力な結晶化剤(結晶核剤、造核剤あるいは結晶化促進剤)の添加が行われている。結晶化剤の添加は、結晶核となる成分が多く配合されることにより、微細な結晶を急速に生成させる作用があり、見かけ上、顔料による収縮への影響を低減させる効果がある。また、結晶化剤を用いることにより、成形サイクルを短くできること、また剛性や透明性が上がる利点などが知られている。結晶化剤としては、例えば、安息香酸ナトリウム、4−第三ブチル安息香酸アルミニウム、アジピン酸ナトリウムなどのカルボン酸金属塩、ナトリウムビス(4−第三ブチルフェニル)ホスフェート、ナトリウム−2,2' −メチレンビス(4,6−ジ第三ブチルフェニル)ホスフェートなどの酸性リン酸エステル金属塩、ジベンジリデンソルビトール、ビス(メチルベンジリデン)ソルビトールなどのソルビトールアセタールタイプが用いられている。しかし、反りや変形に対しては効果が不十分であった。 As another method for improving warpage and deformation, a powerful crystallization agent (crystal nucleating agent, nucleating agent or crystallization accelerator) is added. The addition of the crystallizing agent has the effect of rapidly producing fine crystals by blending many components serving as crystal nuclei, and apparently has the effect of reducing the influence on shrinkage by the pigment. In addition, it is known that the molding cycle can be shortened by using a crystallization agent, and the advantage that rigidity and transparency are increased. Examples of the crystallization agent include carboxylic acid metal salts such as sodium benzoate, aluminum 4-tert-butylbenzoate and sodium adipate, sodium bis (4-tert-butylphenyl) phosphate, sodium-2,2′- Acid phosphate metal salts such as methylenebis (4,6-ditert-butylphenyl) phosphate, sorbitol acetal types such as dibenzylidene sorbitol and bis (methylbenzylidene) sorbitol are used. However, the effect was insufficient for warpage and deformation.
また、顔料を改質して結晶核として働かないようにする方法も検討されており、顔料の結晶形、粒子径、形状を変えること、顔料骨格に各種の置換基を導入した顔料誘導体(有機色素化合物)を添加することによる顔料表面の改質、顔料に樹脂やシランカップリング剤等で表面処理を施すことによる顔料表面の改質等が行われている。 In addition, methods for modifying pigments so that they do not function as crystal nuclei are also being studied. Pigment derivatives (organic) with various substituents introduced into the pigment skeleton, changing the crystal form, particle size, and shape of the pigment. The pigment surface is modified by adding a pigment compound), and the pigment surface is modified by subjecting the pigment to a surface treatment with a resin or a silane coupling agent.
顔料の結晶形、粒子径、形状を変える方法としては、特許文献1、特許文献2、特許文献3等に記載されている。しかし、いずれも十分な効果が得られていない。また、顔料の結晶形、粒子径、形状の変化は、色相、分散性、着色力、耐熱性、耐光性等の顔料元来の物性に影響を及ぼしてしまう。 Methods for changing the crystal form, particle size, and shape of the pigment are described in Patent Document 1, Patent Document 2, Patent Document 3, and the like. However, sufficient effects are not obtained. In addition, changes in the crystal form, particle diameter, and shape of the pigment affect the original properties of the pigment such as hue, dispersibility, coloring power, heat resistance, and light resistance.
フタロシアニン顔料のそりや変形の改善の方法としては、日本色材協会誌(2003年)Vol.76 97頁に記載されている方法、すなわちフタロシアニン骨格に特定数のハロゲンを導入する方法が記載されている。この方法では反りや変形は改善されるものの本来フタロシアニン顔料が持つ高着色力、高鮮明などの特性は失われ、また色相も大きく変わってしまう。 As a method for improving warpage and deformation of a phthalocyanine pigment, a method described in Journal of Japan Colorant Association (2003) Vol. 76, page 97, that is, a method of introducing a specific number of halogens into a phthalocyanine skeleton is described. Yes. Although this method improves the warpage and deformation, characteristics such as high coloring power and high sharpness inherent to the phthalocyanine pigment are lost, and the hue is greatly changed.
反りや変形の改善を目的とした、顔料構造に置換基を導入したいわゆる顔料誘導体による表面改質の方法としては、特許文献4、特許文献5にフタルイミドメチル誘導体が記載されている。この発明により、反りや変形は幾分改善されるものの十分ではなく、反りの改善のために必要量を添加すると色移行性が悪化し実用には至っていない。 As a surface modification method using a so-called pigment derivative in which a substituent is introduced into a pigment structure for the purpose of improving warpage and deformation, phthalimidomethyl derivatives are described in Patent Documents 4 and 5. Although the warpage and deformation are somewhat improved by this invention, it is not sufficient, and when a necessary amount is added for improving the warpage, the color transfer property is deteriorated, and it has not been put into practical use.
顔料誘導体以外の顔料の表面改質方法としては、有機シランや有機チタンによる表面処理、熱可塑性樹脂による顔料の表面コーティングが行われている。特許文献6には、有機顔料残基を有するスルホン酸と水溶性高分子アンモニウム塩からなるポリマーとを共存させ、顔料表面をポリマーで改質することが記載されている。しかし、いずれも効果は不十分であった。
本発明はフタロシアニンを用いてプラスチックを着色したときにフタロシアニンがもつ着色剤としての優れた特性を損なわず成形品における反りや変形を解決する顔料組成物および着色剤を提供する。 The present invention provides a pigment composition and a colorant that solves warpage and deformation in a molded article without impairing the excellent properties of the phthalocyanine as a colorant when a plastic is colored with phthalocyanine.
本発明は、 フタロシアニン50〜95重量%、ハロゲン原子の置換基数が1〜9で平均置換基数が2.0〜4.0のハロゲン化フタロシアニン1〜45重量%、および下記一般式(1)もしくは一般式(2)で示されるフタロシアニン誘導体0.1〜10重量%からなる顔料組成物に関する。
一般式(1)
P−(X)m
(式中、Pは銅フタロシアニン骨格を表し、Xは炭素数12〜18のアルキル基、炭素数12〜18のアルコキシ基、−SO2NHR、−SO2NR2 、−NR2 、−CONR2 、−CONHR、−SR(Rは炭素数12〜18のアルキル基またはアルケニル基を表す。)を表し、mは1〜4の整数を表す。)
一般式(2)
(但し、式中Pは銅フタロシアニン骨格を表し、Yは水素もしくはハロゲン原子を表し、nは1〜4の整数を表す。)
The present invention relates to 1 to 45% by weight of halogenated phthalocyanine having 50 to 95% by weight of phthalocyanine, 1 to 9 halogen atom substituents and 2.0 to 4.0 average substituents, and the following general formula (1) or The present invention relates to a pigment composition comprising 0.1 to 10% by weight of a phthalocyanine derivative represented by the general formula (2).
General formula (1)
P- (X) m
(In the formula, P represents a copper phthalocyanine skeleton, X represents an alkyl group having 12 to 18 carbon atoms, an alkoxy group having 12 to 18 carbon atoms, —SO 2 NHR, —SO 2 NR 2 , —NR 2 , —CONR 2. , -CONHR, -SR (R represents an alkyl group or alkenyl group having 12 to 18 carbon atoms), and m represents an integer of 1 to 4.)
General formula (2)
(Wherein, P represents a copper phthalocyanine skeleton, Y represents a hydrogen or halogen atom, and n represents an integer of 1 to 4.)
更に本発明は、上記顔料組成物からなるプラスチック用着色剤である。 Furthermore, the present invention is a colorant for plastics comprising the above pigment composition.
更に本発明は、上記顔料組成物と、脂肪族カルボン酸金属塩または芳香族カルボン酸金属塩とからなる粉体状着色剤である。 Furthermore, the present invention is a powdery colorant comprising the above pigment composition and an aliphatic carboxylic acid metal salt or an aromatic carboxylic acid metal salt.
更に本発明は、プラスチック100重量部に、上記顔料組成物を0.1〜300重量部配合して得られる着色剤である。 Furthermore, this invention is a coloring agent obtained by mix | blending 0.1-300 weight part of said pigment compositions with 100 weight part of plastics .
更に本発明は、上記プラスチックがポリオレフィンである着色剤である。 Furthermore, the present invention is a colorant in which the plastic is a polyolefin.
本発明により、フタロシアニンの持つ鮮やかな色相、発色の特性を有したまま、成形品の反り、変形、寸法変化を小さくすることが出来る。成形品の反りや変形による不良品が減少し、生産性の向上を図ることが出来る。 According to the present invention, it is possible to reduce warpage, deformation, and dimensional change of a molded product while maintaining the vivid hue and color development characteristics of phthalocyanine. Defective products due to warping and deformation of the molded product are reduced, and productivity can be improved.
更に本発明は、上記記載の着色剤をプラスチックに配合してなる成形品である。 Furthermore, the present invention is a molded article obtained by blending the above-described colorant with plastic.
以下に本発明の実施の形態について詳しく説明する。
本発明に用いるフタロシアニンは無金属フタロシアニン、または銅フタロシアニンおよびアルミフタロシアニンなどの金属フタロシアニンであり、中心金属の有無、種類等は特に制限されるものではない。
Hereinafter, embodiments of the present invention will be described in detail.
The phthalocyanine used in the present invention is a metal-free phthalocyanine or a metal phthalocyanine such as copper phthalocyanine and aluminum phthalocyanine, and the presence or absence of the central metal, the type, etc. are not particularly limited.
本発明における一般式(1)および一般式(2)のフタロシアニン構造(P)は銅フタロシアニンである。
Phthalocyanine structure of the general formula (1) and general formula (2) in the present invention (P) is Ru copper phthalocyanine der.
本発明で用いるハロゲン化フタロシアニンの製造方法は、一般的に知られているハロゲン化フタロシアニンの製法であればよく、ハロゲン原子の置換基数が1〜9個と平均置換基数が2.0〜4.0個であれば特に制限はない。製造方法としては、あらかじめハロゲン原子置換基を導入したハロゲン化フタル酸を用い粗製ハロゲン化フタロシアニンを合成する製法や粗製フタロシアニンを塩化アルミ、あるいは塩化アルミと食塩の溶融塩とした状態でハロゲンを導入する、いわゆる塩化アルミ法、ハロゲン化フタロニトリルを用いて粗製ハロゲン化フタロシアニンを合成する製法があげられるが、中でも塩化アルミ法にて得られたハロゲン化フタロシアニンは反りの改良効果が他の方法よりも良好であり、より好ましい。平均ハロゲン置換基数は、導入するハロゲン量を制御することにより行う。導入するハロゲン量は、製法、装置、反応条件により異なるが、ハロゲン量は少ない場合は平均ハロゲン置換基数が少なく、ハロゲン量が多い場合は、平均ハロゲン置換基数が多くなる。導入するハロゲン量が過小である場合は反りの改良効果に関して好ましくなく、過大である場合も反りの改良効果や色相が悪くなるため好ましくない。平均ハロゲン置換基数が2.0〜4.0個となる量が好ましい。 The method for producing a halogenated phthalocyanine used in the present invention may be a generally known method for producing a halogenated phthalocyanine. The halogen atom has 1 to 9 substituents and an average substituent number of 2.0 to 4. If it is 0, there is no restriction in particular. As a production method, a halogen phthalic acid previously introduced with a halogen atom substituent is used to synthesize a crude halogenated phthalocyanine, or a halogen is introduced in a state where the crude phthalocyanine is aluminum chloride or a molten salt of aluminum chloride and sodium chloride. The so-called aluminum chloride method, and a method of synthesizing a crude halogenated phthalocyanine using a halogenated phthalonitrile, are mentioned. Among them, the halogenated phthalocyanine obtained by the aluminum chloride method has a better warping improvement effect than other methods. It is more preferable. The average number of halogen substituents is determined by controlling the amount of halogen introduced. The amount of halogen to be introduced varies depending on the production method, apparatus, and reaction conditions. When the amount of halogen is small, the average number of halogen substituents is small, and when the amount of halogen is large, the number of average halogen substituents is large. When the amount of halogen to be introduced is too small, it is not preferable with respect to the effect of improving the warp, and when it is too large, the effect of improving the warp and the hue are deteriorated. An amount such that the average number of halogen substituents is 2.0 to 4.0 is preferred.
ハロゲン化フタロシアニンは、このまま用いても良いが、より核剤としての働きをなくすために、結晶形を無定型にすることが好ましく、例えば、硫酸を使用したアシドペースティング法による処理等、従来公知の方法で行うことができる。 The halogenated phthalocyanine may be used as it is, but in order to eliminate the function as a nucleating agent, it is preferable to make the crystal form amorphous, for example, conventionally known treatment by acid pasting method using sulfuric acid, etc. It can be done by the method.
本発明において、ハロゲン化フタロシアニンの形態は限定されるものではなく、着色剤やマスターバッチの製法により粉末状あるいは、水ペースト状で使用できる。 In the present invention, the form of the halogenated phthalocyanine is not limited, and the halogenated phthalocyanine can be used in a powder form or a water paste form by a colorant or a masterbatch production method.
本発明の実施の際に用いるハロゲン化フタロシアニンは顔料組成物の中で1〜45重量%用いる事が出来、色相を考えるとさらに好ましくは5〜20重量%用いる事が望ましい。ハロゲン化フタロシアニンの比率が低い場合は反りの改良効果が十分ではなく好ましくなく、逆に多すぎるとフタロシアニンが持つ鮮やかな色相が失われてしまうため好ましくない。 The halogenated phthalocyanine used in the practice of the present invention can be used in an amount of 1 to 45% by weight in the pigment composition, and considering the hue, it is more preferable to use 5 to 20% by weight. When the ratio of the halogenated phthalocyanine is low, the effect of improving the warp is not sufficient and is not preferable. On the other hand, when the amount is too large, the vivid hue of the phthalocyanine is lost.
一般式(1)もしくは一般式(2)で表されるフタロシアニン誘導体はそれぞれ単独で使用した場合も反りの改良効果を得る事が出来るが、そのためには顔料組成物中に10〜20重量%含まれる事が必要であり、反りの改良のために必要量を添加した場合には鮮明性や色相が悪くなるため、単独で使用することは実用上好ましくない。 The phthalocyanine derivative represented by the general formula (1) or the general formula (2) can obtain an effect of improving warpage when used alone, but for that purpose, it is contained in an amount of 10 to 20% by weight in the pigment composition. When a necessary amount is added for improving warpage, the sharpness and hue are deteriorated, and therefore it is not practically preferable to use it alone.
本発明で用いるフタロシアニン誘導体は顔料組成物のうち0.1〜10重量%、さらに好ましくは0.1〜4重量%含まれる事が望ましい。フタロシアニン誘導体は少なすぎると鮮明性や反りの改善効果に対して十分ではなく、逆に10重量%を超えると色相が不鮮明になるため望ましくない。 The phthalocyanine derivative used in the present invention is desirably contained in the pigment composition in an amount of 0.1 to 10% by weight, more preferably 0.1 to 4% by weight. If the amount of the phthalocyanine derivative is too small, it is not sufficient for the effect of improving the sharpness and warpage, and conversely if it exceeds 10% by weight, the hue becomes unclear.
本発明の顔料組成物を構成するハロゲン化フタロシアニンと一般式(1)もしくは一般式(2)で表されるフタロシアニン誘導体は顔料に対して共に用いることにより、ハロゲン化フタロシアニンやフタロシアニン誘導体を単独で用いたものよりも、成形品の反りや変形を小さくする効果が極めて大きく発揮される。 When the halogenated phthalocyanine and the phthalocyanine derivative represented by the general formula (1) or (2) constituting the pigment composition of the present invention are used together with the pigment, the halogenated phthalocyanine or the phthalocyanine derivative is used alone. The effect of reducing the warpage and deformation of the molded product is much greater than that obtained.
フタロシアニンとハロゲン化フタロシアニンおよび一般式(1)もしくは一般式(2)で表されるフタロシアニン誘導体の混合方法は、特に限定されないが、おのおのの粉体をスリーハンズミキサー、ヘンシェルミキサー、タンブラー、ナウターミキサー等の混合機で混合する方法、水や有機溶剤のスラリーとして撹拌混合する方法、3本ロールや2本ロールで媒体と共に練肉する方法、ニーディングや溶剤処理などの顔料化の工程でハロゲン化フタロシアニンおよび一般式(1)もしくは一般式(2)で表されるフタロシアニン誘導体を添加する方法等がある。好ましくは、有機溶剤を用いたスラリー状態で混合する方法が十分な効果を発現するに有利である。 The mixing method of phthalocyanine and halogenated phthalocyanine and the phthalocyanine derivative represented by general formula (1) or general formula (2) is not particularly limited. Halogenation in pigmentation processes such as kneading and solvent treatment, mixing with a mixer such as water, stirring and mixing as a slurry of water or organic solvent, mixing with a medium with three or two rolls There is a method of adding phthalocyanine and a phthalocyanine derivative represented by the general formula (1) or (2). Preferably, a method of mixing in a slurry state using an organic solvent is advantageous for exhibiting a sufficient effect.
本発明のプラスチック用着色剤は、顔料組成物の他に、他の成分として、本発明の効果を阻害しないか、あるいは衛生上問題ない範囲で、他の有機顔料、無機顔料、ワックス、又その誘導体、重金属不活性剤、アルカリ金属、アルカリ土類金属または亜鉛の金属石けん、ハイドロタルサイト、ノニオン系界面活性剤、カチオン系界面活性剤、アニオン系界面活性剤、両性界面活性剤などからなる帯電防止剤、ハロゲン系、リン系または金属酸化物等の難燃剤、エチレンビスアルキルアマイド等の滑剤、酸化防止剤や紫外線吸収剤、加工助剤、充填剤、公知のポリマー用の各種添加剤などを包含させることができる。要求される品質、着色作業性を満足する為に、あらかじめ顔料をこれらの成分と分散処理したもので、粉体状のドライカラー、顆粒状のビーズカラー、液状のペーストカラー、またはリキッドカラーといわれるものである。 In addition to the pigment composition, the colorant for plastics of the present invention may contain other organic pigments, inorganic pigments, waxes, or the like, as other components, as long as they do not impair the effects of the present invention or have no sanitary problems. Charging consisting of derivatives, heavy metal deactivators, alkali metal, alkaline earth metal or zinc metal soaps, hydrotalcite, nonionic surfactants, cationic surfactants, anionic surfactants, amphoteric surfactants, etc. Inhibitors, flame retardants such as halogen-based, phosphorus-based or metal oxides, lubricants such as ethylene bisalkylamide, antioxidants and ultraviolet absorbers, processing aids, fillers, various additives for known polymers, etc. Can be included. In order to satisfy the required quality and workability of coloring, pigment is dispersed in advance with these components, and it is said to be powdery dry color, granular bead color, liquid paste color, or liquid color. Is.
本発明の着色剤の好ましい一つの形態は、ドライカラーと呼ばれる顔料を高濃度に含有する粉末状の着色剤である。ドライカラーの場合、一般的にフタロシアニンとハロゲン化フタロシアニン、一般式(1)もしくは一般式(2)で表されるフタロシアニン誘導体の合計100重量部に対して、脂肪族カルボン酸又は芳香族カルボン酸及びそれらの金属塩を分散剤として1〜1000重量部含有する。脂肪族カルボン酸又は芳香族カルボン酸及びそれらの金属塩の例としては、脂肪族カルボン酸としては、カプリル酸、オレイン酸、ステアリン酸等が挙げられ、芳香族カルボン酸としてはフタル酸、安息香酸等が挙げられ、又金属としては、リチウム、カルシウム、マグネシウム、亜鉛等が挙げられる。ドライカラーは粉末状で作業性は悪いものの、顔料の濃度が高く、少量で着色に寄与する為価格的に最も経済的であり、ポリオレフィンの着色に多く用いられる。成形に供する場合は、成形用プラスチック100重量部に対して、ドライカラー0.001〜10重量部が用いられる。プラスチックのペレットとドライカラーを混合機等で予め均一に混合した後に成形加工に供される。 One preferable form of the colorant of the present invention is a powdery colorant containing a pigment called dry color at a high concentration. In the case of dry color, an aliphatic carboxylic acid or an aromatic carboxylic acid and a phthalocyanine and a halogenated phthalocyanine, and a total of 100 parts by weight of the phthalocyanine derivative represented by the general formula (1) or the general formula (2) 1 to 1000 parts by weight of these metal salts are contained as a dispersant. Examples of aliphatic carboxylic acids or aromatic carboxylic acids and metal salts thereof include caprylic acid, oleic acid, stearic acid and the like as aliphatic carboxylic acids, and phthalic acid and benzoic acid as aromatic carboxylic acids. In addition, examples of the metal include lithium, calcium, magnesium, and zinc. Although the dry color is powdery and has poor workability, it has the highest pigment concentration and contributes to coloring in a small amount, so it is the most economical in terms of price and is often used for coloring polyolefins. When used for molding, 0.001 to 10 parts by weight of a dry color is used with respect to 100 parts by weight of the plastic for molding. The plastic pellets and dry color are uniformly mixed in advance with a mixer or the like, and then subjected to molding.
本発明において、着色されるプラスチックは、加熱により軟化し、冷却により再度、硬化する部分的に結晶性を有する樹脂であり、特にエチレン、プロピレン、ブチレン、スチレンおよび/またはジビニルベンゼンのホモポリマー、あるいはブロックもしくはランダムコポリマーまたはターポリマー、特にHDPE、LDPE、ポリプロピレンおよびポリスチレンのようなα−オレフィン類である。その他の有用な樹脂の例としては、ポリエチレンテレフタレートのようなポリエステル類、ナイロン6、ナイロン66のようなポリアミド類、および熱可塑性アイオノマー類である。本発明の着色剤はこれらの結晶性を有する熱可塑性樹脂に対して高い効果を有し、特に、α−オレフィン、エチレン、プロピレンおよびブチレンのホモポリマー、コポリマー等のいわゆるポリオレフィン樹脂に対し、顕著な効果を有する。 In the present invention, the plastic to be colored is a partially crystalline resin that softens by heating and cures again by cooling, in particular, a homopolymer of ethylene, propylene, butylene, styrene and / or divinylbenzene, or Block or random copolymers or terpolymers, in particular α-olefins such as HDPE, LDPE, polypropylene and polystyrene. Examples of other useful resins are polyesters such as polyethylene terephthalate, polyamides such as nylon 6, nylon 66, and thermoplastic ionomers. The colorant of the present invention has a high effect on these crystalline thermoplastic resins, and is particularly remarkable for so-called polyolefin resins such as α-olefin, ethylene, propylene and butylene homopolymers and copolymers. Has an effect.
ポリオレフィン樹脂としては、MFR(メルトフローレート、すなわち溶解粘度)が0.001〜30のものが好ましい。MFRが0.001未満では着色樹脂組成物の溶融粘度が高過ぎるために成形加工性が悪くなる場合や、成形品にウエルドマークやフローマークが発生する場合がある。一方、MFRが30を越えると、成形品の機械物性の低下が懸念される。特に、高密度ポリエチレンを用いる場合には、MFRが0.005〜10、低密度ポリエチレン、ポリプロピレン、ポリブテンを用いる場合には、MFRが0.005〜20であることが好ましい。 As polyolefin resin, the thing of MFR (melt flow rate, ie, melt viscosity) 0.001-30 is preferable. If the MFR is less than 0.001, the melt viscosity of the colored resin composition is too high, so that moldability may be deteriorated, or a weld mark or a flow mark may be generated in the molded product. On the other hand, when the MFR exceeds 30, there is a concern that the mechanical properties of the molded product may be deteriorated. In particular, when high density polyethylene is used, the MFR is preferably 0.005 to 10, and when low density polyethylene, polypropylene, or polybutene is used, the MFR is preferably 0.005 to 20.
本発明の着色剤は、顔料組成物とプラスチックから構成され顔料を高濃度に含有するいわゆるマスターバッチと称されるペレット状の着色剤であっても良い。そして、顔料を高濃度に含有するマスターバッチの場合には、係わるマスターバッチをプラスチックで希釈して成形に供し、成形品を得ればよい。 The colorant of the present invention may be a pellet-like colorant called a so-called master batch which is composed of a pigment composition and a plastic and contains a pigment in a high concentration. In the case of a master batch containing a pigment at a high concentration, the master batch may be diluted with plastic and used for molding to obtain a molded product.
マスターバッチと着色ペレットを比較すると、加工工程等は大差なく、マスターバッチの方が顔料を高濃度に含有する分、着色ペレットよりややコスト高ではあるが、マスターバッチの場合には安価なプラスチックで0.5〜200倍に希釈して成形品を得るので、最終成形品として比較すると着色ペレットで成形品を得る場合より、マスターバッチを用いてプラスチックで希釈して成形品を得る方が、安価になり好ましい。 Comparing the masterbatch with the colored pellets, the processing steps are not much different, and the masterbatch is a little more expensive than the colored pellets because it contains a higher concentration of pigment. Since a molded product is obtained by diluting 0.5 to 200 times, it is cheaper to obtain a molded product by diluting with plastic using a masterbatch than to obtain a molded product with colored pellets when compared with the final molded product. This is preferable.
マスターバッチの場合は、プラスチック100重量部、本発明の顔料組成物0.1〜300重量部を含有することが好ましい。顔料組成物が0.1重量部未満だとマスターバッチとしての意味合いがなく、300重量部よりも多く顔料組成物を含有するとマスターバッチの造粒が困難になる。そして、顔料を高濃度に含有するマスターバッチの場合には、係るマスターバッチをプラスチックで希釈して成形に供し、成形品を得ればよい。希釈に用いられるプラスチックとしては、顔料を高濃度に含有するペレット状のマスターバッチを得る際に用いられたプラスチックと同様のものが例示できる。なお、最終成形品は、前記した希釈を必要とせずそのまま成形に供されるペレットの場合と同様に、プラスチック100重量部、着色剤0.001〜10重量部を含有することが好ましい。 In the case of a masterbatch, it is preferable to contain 100 parts by weight of plastic and 0.1 to 300 parts by weight of the pigment composition of the present invention. When the pigment composition is less than 0.1 parts by weight, there is no meaning as a master batch, and when the pigment composition is contained in an amount of more than 300 parts by weight, granulation of the master batch becomes difficult. And in the case of the masterbatch which contains a pigment in high concentration, the masterbatch should just be diluted with a plastic, and it may use for shaping | molding and a molded article may be obtained. Examples of the plastic used for dilution include the same plastics used in obtaining a pellet-shaped masterbatch containing a high concentration of pigment. The final molded product preferably contains 100 parts by weight of plastic and 0.001 to 10 parts by weight of a colorant, as in the case of pellets that are directly subjected to molding without requiring dilution.
マスターバッチは、本発明の効果を阻害しないか、あるいは衛生上問題ない範囲で他の有機顔料、無機顔料、他のプラスチック、ワックス、又その誘導体や、重金属不活性剤、アルカリ金属、アルカリ土類金属または亜鉛の金属石けん、ハイドロタルサイト、ノニオン系界面活性剤、カチオン系界面活性剤、アニオン系界面活性剤、両性界面活性剤などからなる帯電防止剤、ハロゲン系、リン系または金属酸化物等の難燃剤、エチレンビスアルキルアマイド等の滑剤、酸化防止剤や紫外線吸収剤、加工助剤、充填剤、公知のポリマー用の各種添加剤などを包含させることができる。 The master batch does not impair the effects of the present invention, or other organic pigments, inorganic pigments, other plastics, waxes, derivatives thereof, heavy metal deactivators, alkali metals, alkaline earths as long as there is no sanitary problem. Metal or zinc metal soap, hydrotalcite, nonionic surfactant, cationic surfactant, anionic surfactant, antistatic agent composed of amphoteric surfactant, halogen-based, phosphorus-based or metal oxide, etc. Flame retardants, lubricants such as ethylene bisalkylamides, antioxidants and ultraviolet absorbers, processing aids, fillers, various additives for known polymers, and the like.
本発明の着色剤を得る際には、顔料組成物とプラスチックを混練する前に、顔料組成物をポリエチレンワックス等の分散剤で処理を行い前加工することが好ましい。前加工する方法としては、単に着色剤と分散剤をミキサーに配合し混合したものと、顔料組成物と分散剤を配合し溶融混練後に粉砕したものがあるが、着色剤の均一分散性の点で、後者の溶融混練を行ったタイプの加工処理方法が好ましい。 When obtaining the colorant of the present invention, it is preferable to pre-process the pigment composition with a dispersant such as polyethylene wax before kneading the pigment composition and the plastic. There are two methods of pre-processing: one in which a colorant and a dispersant are blended in a mixer, and one in which a pigment composition and a dispersant are blended and pulverized after melt-kneading. Thus, the latter type of processing method in which melt kneading is performed is preferable.
本発明において、プラスチックを成形加工して成形品を得る際の成形方法は特に限定されるものではない。射出成形、ブロー成形、インフレーション成形、押出し成形、エンゲル成形、真空成形等、成形方法にかかわらず、着色された成形品の反りや変形を抑制する効果が得られる。 In the present invention, the molding method for molding a plastic to obtain a molded product is not particularly limited. Regardless of the molding method such as injection molding, blow molding, inflation molding, extrusion molding, engel molding, vacuum molding, etc., the effect of suppressing warpage and deformation of the colored molded product can be obtained.
以下、実施例に基づき本発明を更に詳しく説明するが、本発明は実施例に特に限定されるものではない。実施例中、部および%は、特に指定がない場合はそれぞれ重量部、重量%を表す。なお、製造例で得られたハロゲン化フタロシアニンのハロゲン置換基数はマススペクトル(日本電子データム製JMS−DX303HF)により測定した。 EXAMPLES Hereinafter, although this invention is demonstrated in more detail based on an Example, this invention is not specifically limited to an Example. In the examples, parts and% represent parts by weight and% by weight, respectively, unless otherwise specified. The number of halogen substituents of the halogenated phthalocyanine obtained in the production example was measured by mass spectrum (JMS-DX303HF manufactured by JEOL Datum).
反りや変形の評価は、射出成形機にて収縮性評価用の金型(射出方向とその垂直方向に10.00cmの標線が設けられた縦150mm、横120mm、厚さ2mmのプレートを作成する金型)を用いて成形し、成形されたプレートを恒温室で3日保存した後、射出方向とその垂直方向の収縮率の比で計算される収縮差率と、目視で反りや変形の程度を評価した。成形温度は220℃、金型温度40℃で連続20枚射出成形し、評価にはその内、14枚目から19枚目の6枚を用いた。成形されたプレートを恒温室で24時間以上保存した後、精密ノギスにて標準間距離を計測しその値から射出方向とその垂直方向の収縮率を求めた。その後、射出方向とその垂直方向の収縮率の比で計算される収縮差率と、目視で反りや変形の程度を評価した。なお、収縮差率の計算式は式1の通りである。一般的に顔料と樹脂からなる成形プレートと樹脂のみ(以下ナチュラルと呼ぶ)で成形したプレートの収縮差率との差が10%以内に収まれば低収縮顔料または低収縮顔料組成物と呼ばれる。
収縮差率=(射出方向の収縮率−垂直方向の収縮率)/射出方向の収縮率
For evaluation of warpage and deformation, a mold for shrinkage evaluation was created with an injection molding machine (a plate with a length of 150 mm, a width of 120 mm, and a thickness of 2 mm with a marking line of 10.00 cm in the injection direction and its vertical direction) Molds), and the molded plate is stored in a thermostatic chamber for 3 days, and the shrinkage difference calculated by the ratio of the shrinkage rate in the injection direction and its vertical direction, and the warpage and deformation are visually observed. The degree was evaluated. Twenty sheets were continuously injection-molded at a molding temperature of 220 ° C. and a mold temperature of 40 ° C., and six of the fourteenth to nineteenth sheets were used for evaluation. After the molded plate was stored in a temperature-controlled room for 24 hours or more, the distance between the standards was measured with a precision caliper, and the shrinkage rate in the injection direction and the vertical direction was determined from the measured distance. Thereafter, the shrinkage difference rate calculated by the ratio between the injection direction and the shrinkage rate in the vertical direction, and the degree of warpage and deformation were visually evaluated. In addition, the calculation formula of the shrinkage difference rate is as Formula 1. In general, when the difference between the shrinkage difference between a molded plate made of pigment and resin and a plate molded only with resin (hereinafter referred to as natural) is within 10%, it is called a low shrinkage pigment or a low shrinkage pigment composition.
Shrinkage difference rate = (shrinkage rate in the injection direction−shrinkage rate in the vertical direction) / shrinkage rate in the injection direction
目視評価の基準は、プラスチックのみで作成した無色の成形プレート(以下ナチュラルのプレートと称す)と比較して、反りや変形が同程度であれば顔料の影響が見られないとして「良好」、反りや変形が激しいものは「不良」とした。 The standard for visual evaluation is “good”, warping because the effect of the pigment is not seen if the warpage and deformation are comparable compared to a colorless molded plate made of plastic alone (hereinafter referred to as “natural plate”). Those that were severely deformed were considered “bad”.
色相の測定は、それぞれ実施例にて用いた顔料組成物1部、ステアリン酸亜鉛1部、ポリプロピレン1000部、及び酸化チタン50部を十分に混合し、各混合物を単軸押出機にて混練し、得られたコンパウンドを射出成形機にて成形し2mm厚の成形プレートを得た。得られた各プレートの反射率を色差計「KURABOColor−7E」(KURABO社製)を用いて、L*a*b*色相系にて測色した。顔料組成物にLionol Blue FG-7351 (C.I.Pigment Blue 15:3 東洋インキ社製)を用いた比較例1を色相差測定における標準とした。標準との色差を求めΔEが3.0以内の場合かつΔbで2.0以内である場合は「良好」、それ以外は「不良」とした。 Hue was measured by mixing 1 part of the pigment composition used in the examples, 1 part of zinc stearate, 1000 parts of polypropylene, and 50 parts of titanium oxide, and kneading each mixture with a single screw extruder. The obtained compound was molded by an injection molding machine to obtain a molded plate having a thickness of 2 mm. The reflectance of each of the obtained plates was measured using a color difference meter “KURABOColor-7E” (manufactured by KURABO) in an L * a * b * hue system. Comparative Example 1 using Lionol Blue FG-7351 (C.I. Pigment Blue 15: 3 manufactured by Toyo Ink Co., Ltd.) as the pigment composition was used as a standard for measuring the hue difference. The color difference from the standard was determined, and when ΔE was 3.0 or less and Δb was 2.0 or less, it was judged “good”, and otherwise “bad”.
発色強度の測定は、顔料組成物1部、ステアリン酸亜鉛1部、ポリプロピレン1000部、及び酸化チタン50部を十分に混合し、各混合物を単軸押出機にて混練し、得られたコンパウンドを射出成形機にて成形し2mm厚の成形プレートを得た。得られた各プレートの反射率を色差計「KURABOColor−7E」(KURABO社製)を用いて、640nmにおける反射強度を測定し、その反射強度から各プレートのKubelka−Munk関数(k/s)(発色強度)を求めた。発色強度は小数点1位の値を四捨五入した。 The color intensity was measured by mixing 1 part of a pigment composition, 1 part of zinc stearate, 1000 parts of polypropylene, and 50 parts of titanium oxide, kneading each mixture with a single screw extruder, and mixing the resulting compound. Molding was performed by an injection molding machine to obtain a molding plate having a thickness of 2 mm. Using the color difference meter “KURABOColor-7E” (manufactured by KURABO), the reflectance of each plate obtained was measured at 640 nm, and the Kubelka-Munk function (k / s) (k / s) ( Color development intensity) was determined. The color intensity was rounded off to the first decimal place.
以下にハロゲン化フタロシアニンの合成例を製造例1〜4に示す。 Synthesis examples of halogenated phthalocyanines are shown in Production Examples 1 to 4 below.
<製造例1>
塩化アルミニウム200部、食塩40部を加熱して溶融塩とし粗製銅フタロシアニン40部を添加した後、180℃に加熱し、塩素を毎時2部の割合で3時間、合計8部導入した。塩素導入後、反応混合物を多量の水に注入し、ろ過水洗、乾燥、粉砕を行い、46部の塩素化銅フタロシアニンを得た。得られた塩素化銅フタロシアニンを98%硫酸300部に添加し、40〜45℃で4時間攪拌した後、混合物を2000部の水に添加した。80℃で2時間攪拌後、ろ過、水洗、乾燥、粉砕を行い、塩素化銅フタロシアニン45部を得た。塩素化銅フタロシアニンのハロゲン置換基数は1〜6個で、平均置換基数は3.2個であった。
<Production Example 1>
200 parts of aluminum chloride and 40 parts of sodium chloride were heated to form a molten salt, and 40 parts of crude copper phthalocyanine was added, followed by heating to 180 ° C., and introduction of 8 parts of chlorine at a rate of 2 parts per hour for 3 hours. After introducing chlorine, the reaction mixture was poured into a large amount of water, washed with filtered water, dried and pulverized to obtain 46 parts of chlorinated copper phthalocyanine. The obtained chlorinated copper phthalocyanine was added to 300 parts of 98% sulfuric acid and stirred at 40 to 45 ° C. for 4 hours, and then the mixture was added to 2000 parts of water. After stirring at 80 ° C. for 2 hours, filtration, washing with water, drying and pulverization were carried out to obtain 45 parts of chlorinated copper phthalocyanine. The number of halogen substituents of chlorinated copper phthalocyanine was 1 to 6, and the average number of substituents was 3.2.
<製造例2>
塩化アルミニウム200部、食塩40部を加熱して溶融塩とし粗製銅フタロシアニン40部を添加した後、180℃に加熱し、臭素を毎時3部の割合で5時間、合計18部を滴下した。臭素滴下後、反応混合物を多量の水に注入し、ろ過水洗、乾燥、粉砕を行い、55部の臭素化銅フタロシアニンを得た。得られた塩素化銅フタロシアニンを98%硫酸300部に添加し、40〜45℃で4時間攪拌した後、混合物を2000部の水に添加した。80℃で2時間攪拌後、ろ過、水洗、乾燥、粉砕を行い、臭素化銅フタロシアニン52部を得た。臭素化銅フタロシアニンのハロゲン置換基数は1〜5個で、平均置換基数は2.8個であった。
<Production Example 2>
200 parts of aluminum chloride and 40 parts of sodium chloride were heated to form a molten salt, and 40 parts of crude copper phthalocyanine was added, followed by heating to 180 ° C., and bromine was added dropwise at a rate of 3 parts per hour for a total of 18 parts. After dropping bromine, the reaction mixture was poured into a large amount of water, washed with filtered water, dried and pulverized to obtain 55 parts of brominated copper phthalocyanine. The obtained chlorinated copper phthalocyanine was added to 300 parts of 98% sulfuric acid and stirred at 40 to 45 ° C. for 4 hours, and then the mixture was added to 2000 parts of water. After stirring at 80 ° C. for 2 hours, filtration, washing with water, drying and pulverization were carried out to obtain 52 parts of brominated copper phthalocyanine. The number of halogen substituents of brominated copper phthalocyanine was 1 to 5, and the average number of substituents was 2.8.
<製造例3>
塩化アルミニウム200部、食塩40部を加熱して溶融塩とし粗製銅フタロシアニン40部を添加した後、180℃に加熱し、塩素を毎時2部の割合で10時間、合計22部導入した。塩素導入後、反応混合物を多量の水に注入し、ろ過水洗、乾燥、粉砕を行い、58部の塩素化銅フタロシアニンを得た。得られた塩素化銅フタロシアニンを98%硫酸300部に添加し、40〜45℃で4時間攪拌した後、混合物を2000部の水に添加した。80℃で2時間攪拌後、ろ過、水洗、乾燥、粉砕を行い、塩素化銅フタロシアニン57部を得た。塩素化銅フタロシアニンのハロゲン置換基数は5〜11個で、平均置換基数は8.0個であった。
<Production Example 3>
200 parts of aluminum chloride and 40 parts of sodium chloride were heated to form a molten salt, and 40 parts of crude copper phthalocyanine was added, followed by heating to 180 ° C., and introduction of 22 parts of chlorine at a rate of 2 parts per hour for 10 hours. After introducing chlorine, the reaction mixture was poured into a large amount of water, washed with filtered water, dried and pulverized to obtain 58 parts of chlorinated copper phthalocyanine. The obtained chlorinated copper phthalocyanine was added to 300 parts of 98% sulfuric acid and stirred at 40 to 45 ° C. for 4 hours, and then the mixture was added to 2000 parts of water. After stirring at 80 ° C. for 2 hours, filtration, washing with water, drying and pulverization were carried out to obtain 57 parts of chlorinated copper phthalocyanine. The number of halogen substituents of chlorinated copper phthalocyanine was 5 to 11, and the average number of substituents was 8.0.
<製造例4>
塩化アルミニウム200部、食塩40部を加熱して溶融塩とし粗製銅フタロシアニン40部を添加した後、180℃に加熱し、臭素を毎時6部の割合で6時間、合計42部を滴下した。臭素滴下後、塩素を毎時2部の割合で9時間、合計20部導入した。塩素導入後、反応混合物を多量の水に注入し、ろ過水洗、乾燥、粉砕を行い、92部の臭素化塩素化銅フタロシアニンを得た。得られた臭素化塩素化銅フタロシアニンを98%硫酸600部に添加し、40〜45℃で4時間攪拌した後、混合物を4000部の水に添加した。80℃で2時間攪拌後、ろ過、水洗、乾燥、粉砕を行い、臭素化塩素化銅フタロシアニン90部を得た。臭素化塩素化銅フタロシアニンのハロゲン置換基数は12〜16個で、平均置換基数は14.5個であった。
<Production Example 4>
200 parts of aluminum chloride and 40 parts of sodium chloride were heated to form a molten salt, and 40 parts of crude copper phthalocyanine was added, followed by heating to 180 ° C., and bromine was added dropwise at a rate of 6 parts per hour for a total of 42 parts. After dropwise addition of bromine, 20 parts of chlorine was introduced at a rate of 2 parts per hour for 9 hours. After introducing chlorine, the reaction mixture was poured into a large amount of water, washed with filtered water, dried and pulverized to obtain 92 parts of brominated chlorinated copper phthalocyanine. The resulting brominated chlorinated copper phthalocyanine was added to 600 parts of 98% sulfuric acid and stirred at 40-45 ° C. for 4 hours, and then the mixture was added to 4000 parts of water. After stirring at 80 ° C. for 2 hours, filtration, washing with water, drying and pulverization were carried out to obtain 90 parts of brominated chlorinated copper phthalocyanine. The number of halogen substituents of brominated chlorinated copper phthalocyanine was 12 to 16, and the average number of substituents was 14.5.
<実施例1> フタロシアニン顔料(C.I.Pigment Blue 15;3、商品名Lionol Blue FG-7351、東洋インキ製造(株)社製)88部、製造例1に準じて製造したハロゲン化フタロシアニン10部、化合物Aに示すフタロシアニン誘導体2部を混合機にて混合し、顔料組成物を得た。次に、この顔料組成物100部とステアリン酸カルシウム100部を混合機にて混合し着色剤をえた。得られた着色剤2部を高密度ポリエチレン樹脂(製品名Hizex2100J
三井住友ポリオレフィン社製)1000部、付着剤数滴をタンブリングして十分に混合した後、射出成形機でプレート状に成形し、反りや変形、色相を評価した。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視でも反りや変形は同じ程度であった。また色相もフタロシアニン顔料のみで着色したプレート同様色相良好、高着色力のプレートであった。
化合物A
After 1000 parts of Sumitomo Mitsui Polyolefin Co., Ltd. and several drops of adhesive were tumbled and mixed well, they were molded into a plate shape with an injection molding machine, and warpage, deformation, and hue were evaluated. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. Also, the hue was a plate with good hue and high tinting strength similar to the plate colored with phthalocyanine pigment alone.
Compound A
<比較例1> 実施例1において、ハロゲン化フタロシアニン、フタロシアニン誘導体を用いずに、それ以外は同様の方法により成形プレートを作成した。ナチュラルのプレートと比較して、収縮差率の値は大きく、目視でも反りや変形が大きかった。 <Comparative Example 1> A molded plate was prepared in the same manner as in Example 1 except that the halogenated phthalocyanine and the phthalocyanine derivative were not used. Compared to the natural plate, the shrinkage difference rate was large, and the warpage and deformation were large even visually.
<比較例2> 実施例1において、フタロシアニン誘導体を用いずに、それ以外は同様の方法により成形プレートを作成した。ナチュラルのプレートや実施例1と比較して、収縮差率は大きく、目視でも反りや変形が大きかった。 <Comparative example 2> In Example 1, the molding plate was created by the same method except not using a phthalocyanine derivative. Compared with the natural plate and Example 1, the shrinkage difference rate was large, and warping and deformation were large even visually.
<比較例3> 実施例1において、ハロゲン化フタロシアニンを用いなかったこと以外は、同様の方法により成形プレートを作成した。ナチュラルのプレートや実施例1と比較して、収縮差率は大きく、目視でも反りや変形が大きかった。 <Comparative example 3> In Example 1, the shaping | molding plate was created by the same method except not using halogenated phthalocyanine. Compared with the natural plate and Example 1, the shrinkage difference rate was large, and warping and deformation were large even visually.
<比較例4> 実施例1において、ハロゲン化フタロシアニンを用いずに、フタロシアニン誘導体は20部用いて、それ以外は同様の方法により成形プレートを作成した。収縮差率は小さく、目視でも反りは見られなかったが、色相は不良であり、発色も比較対象に比べ95%と優れなかった。 <Comparative example 4> In Example 1, 20 parts of phthalocyanine derivatives were used without using a halogenated phthalocyanine, and a molded plate was prepared in the same manner except that. Although the shrinkage difference was small and no warping was observed visually, the hue was poor and the color development was not as good as 95% compared to the comparative object.
<比較例5> 実施例1において、顔料組成物の変わりに製造例1に準じて製造されたハロゲン化フタロシアニン100部を用いた以外は同様の方法にて成形プレートを得た。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視でも反りや変形は同じ程度であった。しかしながら色相は不良であり、発色も比較対象に比べ90%と優れなかった。 <Comparative Example 5> A molded plate was obtained in the same manner as in Example 1, except that 100 parts of halogenated phthalocyanine produced according to Production Example 1 was used instead of the pigment composition. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. However, the hue was poor, and the color development was not as excellent as 90% compared to the comparative object.
<実施例2> 実施例1において高密度ポリエチレン樹脂(製品名 Hizex2100J 三井住友ポリオレフィン社製)のかわりにポリプロピレン樹脂(製品名 ミツイスミトモPP 三井住友ポリオレフィン社製)を用いた以外は同様の方法で成形プレートを得た。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視でも反りや変形は同じ程度であった。また色相も良好、着色力も比較対象と同等であった。 <Example 2> Molding was performed in the same manner as in Example 1 except that a polypropylene resin (product name: Mitsumi Mitomo PP, manufactured by Sumitomo Mitsui Polyolefin Co., Ltd.) was used instead of the high-density polyethylene resin (product name: Hizex2100J, manufactured by Sumitomo Mitsui Polyolefin) A plate was obtained. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. Also, the hue was good and the coloring power was equivalent to that of the comparative object.
<比較例6> 実施例2において、ハロゲン化フタロシアニン、フタロシアニン誘導体を用いずに、それ以外は同様の方法により成形プレートを作成した。ナチュラルのプレートと比較して、収縮差率の値は大きく、目視でも反りや変形が大きかった。 <Comparative Example 6> A molded plate was prepared in the same manner as in Example 2 except that the halogenated phthalocyanine and the phthalocyanine derivative were not used. Compared to the natural plate, the shrinkage difference rate was large, and the warpage and deformation were large even visually.
<比較例7> 実施例2において、フタロシアニン誘導体を用いずに、それ以外は同様の方法により成形プレートを作成した。ナチュラルのプレートや実施例1と比較して、収縮差率は大きく、目視でも反りや変形が大きかった。 <Comparative example 7> In Example 2, the molding plate was created by the same method except not using a phthalocyanine derivative. Compared with the natural plate and Example 1, the shrinkage difference rate was large, and warping and deformation were large even visually.
<比較例8> 実施例2において、ハロゲン化フタロシアニンを用いなかったこと以外は、同様の方法により成形プレートを作成した。ナチュラルのプレートや実施例1と比較して、収縮差率は大きく、目視でも反りや変形が大きかった。 <Comparative example 8> In Example 2, the shaping | molding plate was created by the same method except not using halogenated phthalocyanine. Compared with the natural plate and Example 1, the shrinkage difference rate was large, and warping and deformation were large even visually.
<実施例3> 実施例1において、ハロゲン化フタロシアニンを製造例2に準じて製造したハロゲン化フタロシアニンに置き換えた以外は、同様の方法により成形プレートを作成した。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視では反りや変形は同程度であった。また色相も良好、着色力も比較対象と同等であった。 <Example 3> A molded plate was produced in the same manner as in Example 1, except that the halogenated phthalocyanine was replaced with the halogenated phthalocyanine produced according to Production Example 2. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. Also, the hue was good and the coloring power was equivalent to that of the comparative object.
<比較例9〜10> 実施例3において、ハロゲン化フタロシアニンをそれぞれ比較例9の場合、製造例3に準じて製造されたハロゲン化フタロシアニン、比較例10の場合、製造例4に準じて製造されたハロゲン化フタロシアニンを用いた以外は、同様の方法により成形プレートを得た。それぞれ収縮差率が大きく、目視でも反りや変形が大きかった。また色相も不良であった。 <Comparative Examples 9 to 10> In Example 3, the halogenated phthalocyanine was produced in accordance with Production Example 3 in the case of Comparative Example 9, and the production in accordance with Production Example 4 in the case of Comparative Example 10. A molded plate was obtained in the same manner except that the halogenated phthalocyanine was used. Each of them had a large shrinkage difference rate, and warping and deformation were also large visually. The hue was also poor.
<実施例4〜11> 実施例1において用いたフタロシアニン誘導体をそれぞれ以下に示す化学物のフタロシアニン誘導体に置き換えた以外は、同様の方法により成形プレートを作成した。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視では反りや変形は同程度であった。また色相も良好、着色力も比較対象と同等であった。
実施例4:
化合物B
化合物C
化合物D
化合物E
化合物F
化合物G
化合物H
化合物I
Example 4:
Compound B
Compound C
Compound D
Compound E
Compound F
Compound G
Compound H
Compound I
<実施例12> フタロシアニン顔料(C.I.Pigment Blue
15;3、商品名Lionol Blue FG-7351、東洋インキ製造(株)社製)88部、製造例1に準じて製造したハロゲン化フタロシアニン10部、化合物Aに示すフタロシアニン誘導体2部を混合機にて混合し、顔料組成物を得た。その顔料組成物100部とポリエチレンワックス(商品名:ハイワックス NL-500、三井化学社製)を十分に混合した後、3本ロールにて溶融混練後粉砕して加工顔料とした。この加工顔料4部と高密度ポリエチレン100部とを混合後、2軸押出機にて溶融混練し、ペレット状のマスターバッチとした。次に、このマスターバッチ5部、高密度ポリエチレン樹脂(製品名Hizex2100J 三井住友ポリオレフィン社製)100部を混合後、射出成形機で実施例1と同様にプレート状に射出成形し、同様に評価した。ナチュラルのプレートや実施例1と比較して、収縮差率は近い値を示し、目視では反りや変形は同程度であった。
化合物A
15; 3, product name Lionol Blue FG-7351, manufactured by Toyo Ink Manufacturing Co., Ltd.) 88 parts, halogenated phthalocyanine 10 parts produced according to Production Example 1, 2 parts phthalocyanine derivative shown in Compound A To obtain a pigment composition. 100 parts of the pigment composition and polyethylene wax (trade name: High Wax NL-500, manufactured by Mitsui Chemicals) were sufficiently mixed, melt-kneaded with three rolls and pulverized to obtain a processed pigment. 4 parts of this processed pigment and 100 parts of high-density polyethylene were mixed and then melt-kneaded with a twin-screw extruder to obtain a pellet master batch. Next, after mixing 5 parts of this master batch and 100 parts of high-density polyethylene resin (product name Hizex 2100J, manufactured by Sumitomo Mitsui Polyolefin Co., Ltd.), it was injection-molded in the same manner as in Example 1 with an injection molding machine and evaluated in the same manner. . Compared with the natural plate and Example 1, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually.
Compound A
<実施例13> 実施例1において、用いた顔料をフタロシアニン顔料(C.I.Pigment Blue 15:1、商品名Lionol Blue 7110-V、東洋インキ製造(株)社製)に置き換えた以外は同様の方法で成形プレートを得た。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視でも反りや変形は同じ程度であった。また色相もフタロシアニン顔料のみで着色したプレート同様色相良好、高着色力のプレートであった。 <Example 13> In the same manner as in Example 1, except that the pigment used was replaced with a phthalocyanine pigment (CIPigment Blue 15: 1, trade name Lionol Blue 7110-V, manufactured by Toyo Ink Manufacturing Co., Ltd.). A molded plate was obtained. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. Also, the hue was a plate with good hue and high tinting strength similar to the plate colored with phthalocyanine pigment alone.
<実施例14> フタロシアニン顔料(C.I.Pigment Blue
15;3、商品名Lionol Blue FG-7351、東洋インキ製造(株)社製)88部、製造例1に準じて製造したハロゲン化フタロシアニン10部、化合物Aに示すフタロシアニン誘導体2部を混合機にて混合し、顔料組成物を得た。得られた顔料組成物1部、ステアリン酸マグネシウム1部、ポリエチレンテレフタレート樹脂(商品名 VylopetEMC-307 東洋紡績社製)を1000部混合し、射出条件を成形温度275℃、金型温度85℃に設定された射出成形機にて成形し、成形プレートを得た。ナチュラルのプレートと比較して、収縮差率は近い値を示し、目視でも反りや変形は同じ程度であった。また色相もフタロシアニン顔料のみで着色したプレート同様色相良好、高着色力のプレートであった。
化合物A
15; 3, product name Lionol Blue FG-7351, manufactured by Toyo Ink Manufacturing Co., Ltd.) 88 parts, halogenated phthalocyanine 10 parts produced according to Production Example 1, 2 parts phthalocyanine derivative shown in Compound A To obtain a pigment composition. 1 part of the obtained pigment composition, 1 part of magnesium stearate and 1000 parts of polyethylene terephthalate resin (trade name VylopetEMC-307, manufactured by Toyobo Co., Ltd.) are mixed, and the injection conditions are set to a molding temperature of 275 ° C. and a mold temperature of 85 ° C. The molded plate was obtained by molding with the injection molding machine. Compared with the natural plate, the shrinkage difference rate showed a close value, and the warpage and deformation were the same level visually. Also, the hue was a plate with good hue and high tinting strength similar to the plate colored with phthalocyanine pigment alone.
Compound A
<比較例11> 実施例9において、ハロゲン化フタロシアニンとフタロシアニン誘導体を用いずに、それ以外は実施例9と同様の方法で成形プレートを得た。ナチュラルのプレートに比べて、収縮差率は大きい値を示し、目視でも反りや変形が大きかった。 <Comparative Example 11> A molded plate was obtained in the same manner as in Example 9 except that halogenated phthalocyanine and a phthalocyanine derivative were not used. Compared to the natural plate, the shrinkage difference rate was large, and the warpage and deformation were large even visually.
実施例1〜14、比較例1〜11までの結果を表1に示す。
Claims (6)
一般式(1)
P−(X)m
(式中、Pは銅フタロシアニン骨格を表し、Xは炭素数12〜18のアルキル基、炭素数12〜18のアルコキシ基、−SO2NHR、−SO2NR2 、−NR2 、−CONR2 、−CONHR、−SR(Rは炭素数12〜18のアルキル基またはアルケニル基を表す。)を表し、mは1〜4の整数を表す。)
一般式(2)
(但し、式中Pは銅フタロシアニン骨格を表し、Yは水素もしくはハロゲン原子を表し、nは1〜4の整数を表す。) 50 to 95% by weight of phthalocyanine, 1 to 45% by weight of halogenated phthalocyanine having 1 to 9 halogen atoms and an average number of substituents of 2.0 to 4.0, and the following general formula (1) or general formula (2 The pigment composition which consists of 0.1-10 weight% of copper phthalocyanine derivatives shown by this.
General formula (1)
P- (X) m
(In the formula, P represents a copper phthalocyanine skeleton, X represents an alkyl group having 12 to 18 carbon atoms, an alkoxy group having 12 to 18 carbon atoms, —SO 2 NHR, —SO 2 NR 2 , —NR 2 , —CONR 2. , -CONHR, -SR (R represents an alkyl group or alkenyl group having 12 to 18 carbon atoms), and m represents an integer of 1 to 4.)
General formula (2)
(However, P in the formula represents a copper phthalocyanine skeleton, Y represents hydrogen also properly represents a C androgenic atoms, n is an integer of 1-4.)
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|---|---|---|---|---|
| US949739A (en) * | 1910-02-15 | Bataille & Co A | Folding gate. | |
| US2861005A (en) * | 1953-11-12 | 1958-11-18 | Du Pont | Phthalocyanine pigments |
| JPS5549634B2 (en) * | 1973-10-26 | 1980-12-12 | ||
| FR2278739A1 (en) * | 1974-07-19 | 1976-02-13 | Ugine Kuhlmann | CRYSTALLIZATION STABLE PHTHALOCYANIN PIGMENTS |
| JPS5145149A (en) * | 1974-10-16 | 1976-04-17 | Dainichiseika Color Chem | HORIOREFUINYOCHAKUSHOKUZAI |
| JPS5650741B2 (en) * | 1974-11-20 | 1981-12-01 | ||
| JPS52124039A (en) * | 1976-04-13 | 1977-10-18 | Dainichi Seika Kogyo Kk | Colorants for polyolefins |
| JPS5941461B2 (en) * | 1976-10-20 | 1984-10-06 | 住友化学工業株式会社 | How to color ABS resin |
| JPS59102958A (en) * | 1982-12-03 | 1984-06-14 | Sumitomo Chem Co Ltd | Preparation of copper phthalocyanine pigment |
| JPH0625295B2 (en) * | 1985-12-03 | 1994-04-06 | 東洋インキ製造株式会社 | Method for coloring polyester resin |
| JP2587293B2 (en) * | 1989-06-12 | 1997-03-05 | 東洋インキ製造株式会社 | Colorant for thermoplastic resin |
| CH685162A5 (en) * | 1991-05-07 | 1995-04-13 | Ciba Geigy Ag | Pigment compositions. |
-
2004
- 2004-06-11 JP JP2004173818A patent/JP4525191B2/en not_active Expired - Lifetime
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| Publication number | Publication date |
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| JP2005023310A (en) | 2005-01-27 |
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