JPH0625295B2 - Method for coloring polyester resin - Google Patents

Method for coloring polyester resin

Info

Publication number
JPH0625295B2
JPH0625295B2 JP60270655A JP27065585A JPH0625295B2 JP H0625295 B2 JPH0625295 B2 JP H0625295B2 JP 60270655 A JP60270655 A JP 60270655A JP 27065585 A JP27065585 A JP 27065585A JP H0625295 B2 JPH0625295 B2 JP H0625295B2
Authority
JP
Japan
Prior art keywords
copper phthalocyanine
coloring
polyester resin
parts
halogenated
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
JP60270655A
Other languages
Japanese (ja)
Other versions
JPS62131054A (en
Inventor
満洲彦 前嶋
信至 木代
與志雄 寺田
隆義 石上
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.)
Toyo Ink Mfg Co Ltd
Original Assignee
Toyo Ink Mfg 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 Toyo Ink Mfg Co Ltd filed Critical Toyo Ink Mfg Co Ltd
Priority to JP60270655A priority Critical patent/JPH0625295B2/en
Publication of JPS62131054A publication Critical patent/JPS62131054A/en
Publication of JPH0625295B2 publication Critical patent/JPH0625295B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Description

【発明の詳細な説明】 「発明の目的」 (産業上の利用分野) 本発明はポリエステル樹脂を着色する方法に関する。さ
らに詳しくは銅フタロシアニンを用いたポリエステル樹
脂の着色において,着色力,着色むら,非凝集性,など
に優れた着色方法に関する。
DETAILED DESCRIPTION OF THE INVENTION "Object of the Invention" (Field of Industrial Application) The present invention relates to a method for coloring a polyester resin. More specifically, the present invention relates to a coloring method excellent in coloring power, uneven coloring, non-aggregating property, etc. in coloring a polyester resin using copper phthalocyanine.

(従来の技術) 従来,銅フタロシアニンおよびもしくはハロゲン化銅フ
タロシアニン顔料は,色調が美しいこと,着色力が大き
いこと,および各種堅牢度が優れているなど広く使用さ
れている顔料であるが,ポリエステル樹脂の着色におい
ては,まだまだ満足出来ない性質が見られる。
(Prior Art) Conventionally, copper phthalocyanine and / or halogenated copper phthalocyanine pigments have been widely used because of their beautiful color tone, high tinting strength, and various fastnesses. In terms of coloring, there are still unsatisfactory properties.

ポリエステル樹脂には,シートモールディングコンパウ
ンで代表される不飽和ポリエステル樹脂と,溶融紡糸で
代表される熱可塑性樹脂(飽和ポリエステル樹脂)があ
るが,これらの樹脂の着色において,着色力がある,着
色むらが少ない,凝集体が少ない,溶融紡糸において糸
切れがない銅フタロシアニンおよびもしくはハロゲン化
銅フタロシアニン顔料の開発が強く要望されている。
Polyester resins include unsaturated polyester resins typified by sheet molding compounds and thermoplastic resins (saturated polyester resins) typified by melt spinning. In coloring these resins, there is coloring power and uneven coloring. There is a strong demand for the development of a copper phthalocyanine and / or a halogenated copper phthalocyanine pigment which has a low content of agglomerates, a small amount of agglomerates, and is free from yarn breakage in melt spinning.

銅フタロシアニンまたはハロゲン化銅フタロシアニン顔
料の欠点の一つは集合性である。銅フタロシアニンまた
はハロゲン化銅フタロシアニン顔料でポリエステル樹脂
を着色したとき,集合性が極めて強いことに起因して起
こる現象として,具体的にはポリエステル樹脂またはコ
ンパウンド中で顔料粒子自体が凝集を生じ,その結果得
られた着色成形物は着色むらを生じ,着色力が著しく低
い成形物しか得られない欠点や,溶融紡糸時フィルター
の目詰りおよび樹脂劣化によって生じる糸切れなどの作
業性の低下と紡糸物の着色力の低下もしくは不均一さが
見られるなどの欠点がある。
One of the drawbacks of copper phthalocyanine or halogenated copper phthalocyanine pigments is the aggregation. When a polyester resin is colored with a copper phthalocyanine or a halogenated copper phthalocyanine pigment, a phenomenon caused by the extremely strong aggregation property, specifically, the pigment particles themselves aggregate in the polyester resin or the compound, and as a result, The obtained colored molded product causes uneven coloring, and only a molded product with extremely low coloring power is obtained. Also, the workability is deteriorated such as clogging of the filter during melt-spinning and yarn breakage caused by resin deterioration and the spinning product. There are drawbacks such as a decrease in coloring power or unevenness.

他方銅フタロシアニン顔料のもう一つの大きい欠点は,
芳香族系溶剤中または高温の条件下で結晶転移および結
晶成長を示すという性質がある。ポリエステル樹脂にお
いては,溶剤溶液としたり、溶融紡糸の如く高温処理さ
れることがあり,銅フタロシアニン顔料が結晶成長する
ことにより,ポリエステル樹脂の着色への適用が制限さ
れることがある。
On the other hand, another major drawback of copper phthalocyanine pigments is
It has the property of exhibiting crystal transition and crystal growth in an aromatic solvent or under high temperature conditions. The polyester resin may be used as a solvent solution or may be subjected to high temperature treatment such as melt spinning, and the copper phthalocyanine pigment may be crystallized to limit its application to coloring the polyester resin.

(発明が解決しようとする問題点) ポリエステル樹脂を青〜緑に着色するに際し,銅フタロ
シアニンおよびもしくはハロゲン化銅フタロシアニン顔
料を使用し,着色力がある,着色むらが少ない,凝集体
が少ない,溶融紡糸において糸切れがない,などに優れ
た着色方法が望まれていた。
(Problems to be solved by the invention) When coloring a polyester resin from blue to green, copper phthalocyanine and / or halogenated copper phthalocyanine pigment is used, and it has coloring power, little coloring unevenness, few aggregates, and melting. There has been a demand for an excellent coloring method that does not cause yarn breakage during spinning.

「発明の構成」 (問題を解決するための手段) 本発明は、ポリエステル樹脂を着色する際して,銅フタ
ロシアニンおよびもしくはハロゲン化銅フタロシアニン
100重量部および下記一般式〔I〕で示される銅フタ
ロシアニン誘導体0.5〜30重量部を用いる着色方法で
ある。
"Structure of the Invention" (Means for Solving the Problem) The present invention relates to 100 parts by weight of copper phthalocyanine and / or halogenated copper phthalocyanine and a copper phthalocyanine represented by the following general formula [I] when coloring a polyester resin. This is a coloring method using 0.5 to 30 parts by weight of the derivative.

一般式〔I〕 (式中,CuPcは銅フタロシアニン残基,Xはハロゲン原
子,Aは基-(CH2)k-,-CH2NH(CH2) −,-CH2NHCO(CH2)
−,-SO2NH(CH2) −,(ただし、R,Rはアル
キル基またはRとRとで少なくとも窒素原子を含む
6員環を示す。),mは0〜10,nは1〜8,kは1〜
2,は1〜4の整数をそれぞれ表す。) 本発明の着色方法により,ポリエステル樹脂の均一な着
色成形物または溶融紡糸物を得ることが出来ることを見
出した。
General formula [I](In the formula, CuPc is a copper phthalocyanine residue, and X is a halogen source.
Child, A is group- (CH2)k-,-CH2NH (CH2) -,-CH2NHCO (CH2)
-,-SO2NH (CH2) -, (However, R1, RTwoIs al
Kill group or R1And RTwoAnd contains at least a nitrogen atom
Indicates a 6-membered ring. ), M is 0 to 10, n is 1 to 8, and k is 1
2 represents an integer of 1 to 4, respectively. ) By the coloring method of the present invention, a uniform coating of polyester resin is achieved.
See that you can get color molded or melt spun
I put it out.

銅フタロシアニン顔料にはβ型銅フタロシアニン(有機
溶剤安定型),α型銅フタロシアニン(有機溶剤不安定
型)を始め,γ型,δ型またはε型などの各種結晶形の
銅フタロシアニン顔料があるが,ポリエステル樹脂の着
色または加工条件である,280〜290℃では,β型
銅フタロシアニンは,結晶が成長することがあり、α型
銅フタロシアニンではβ型への結晶転移を起こしたり,
また同時にβ型での結晶成長が起こり,その結果として
得られたポリエステル樹脂の成形物,紡糸物において色
相の変化および着色力の低下などをよぎなくされてい
た。本発明はこれらの欠点を除去し,良好なポリエステ
ル樹脂の着色成形物または紡糸物などを提供するもので
ある。
Copper phthalocyanine pigments include β-type copper phthalocyanine (organic solvent stable type), α type copper phthalocyanine (organic solvent unstable type), and various crystal form copper phthalocyanine pigments such as γ type, δ type or ε type. At 280 to 290 ° C., which is the coloring or processing condition of the polyester resin, crystals of β-type copper phthalocyanine may grow, and α-type copper phthalocyanine causes a crystal transition to β-type,
At the same time, β-type crystal growth occurred, resulting in a change in hue and a decrease in coloring power in the molded product and spun product of the polyester resin. The present invention eliminates these drawbacks and provides a good colored molded product or spun product of a polyester resin.

本発明の銅フタロシアニンとしては,α型、β型,また
はその他の結晶形のものでよく,一方ハロゲン化銅フタ
ロシアニンとしては、1個または2個のハロゲン原子で
置換された低ハロゲン化銅フタロシアニンから高塩素化
銅フタロシアニン,高臭素化銅フタロシアニン,あるい
はこれらの混合物が挙げられる。また,青味の銅フタロ
シアニン誘導体を高ハロゲン化銅フタロシアニンに混合
することも可能であるが、混合すると色相が青味不鮮明
になる欠点が有るので、高ハロゲン化銅フタロシアニン
には緑色の銅フタロシアニン誘導体を混合することが好
ましく,出来る限りそれぞれの銅フタロシアニン,ハロ
ゲン化銅フタロシアニンに近い色相の銅フタロシアニン
誘導体を用いることが、色相,鮮明性の点から有利であ
る。
The copper phthalocyanine of the present invention may be of α-type, β-type, or other crystalline form, while the halogenated copper phthalocyanine may be a low-halogenated copper phthalocyanine substituted with 1 or 2 halogen atoms. Examples include highly chlorinated copper phthalocyanine, highly brominated copper phthalocyanine, or a mixture thereof. It is also possible to mix a bluish copper phthalocyanine derivative with a highly halogenated copper phthalocyanine, but when mixed, there is a disadvantage that the hue becomes bluish, so the highly halogenated copper phthalocyanine derivative is a green copper phthalocyanine derivative. Are preferably mixed, and it is advantageous from the viewpoint of hue and sharpness to use a copper phthalocyanine derivative having a hue close to that of each copper phthalocyanine or halogenated copper phthalocyanine as much as possible.

一般式〔I〕で表される銅フタロシアニン誘導体の基A
としては,-CH2-,-(CH2)2-,-CH2NH(CH2)4-,-CH2NHCOCH2
-,-CH2NHCO(CH2)4-,-SO2NHCH2-,-SO2NH(CH2)4-などであ
る。基Xは臭素原子およびまたは塩素原子を表わし,こ
れらの置換基数は,その合計が0〜12の数である。0
〜4の範囲では青色となり,緑色の高ハロゲン化銅フタ
ロシアニンに混合する場合には,その量を少なくするこ
とが好ましい。合計数が11〜12の範囲のハロゲン化
銅フタロシアニンでは一般に製造条件が過酷となり副生
成物を生じ易いので,合計数が5〜10の範囲のハロゲ
ン化銅フタロシアニンを緑色の高ハロゲン化銅フタロシ
アニンに混合することが実用上有利である。また同一の
置換基数においては塩素に比較して臭素置換の誘導体
は,黄色を帯びた緑色となる。なお,合成された銅フタ
ロシアニン誘導体における置換基数は,実測すると一般
にいくつかの置換基数のものが混じっているため、それ
らの平均数となる。
Group A of the copper phthalocyanine derivative represented by the general formula [I]
Is -CH 2 -,-(CH 2 ) 2 -,-CH 2 NH (CH 2 ) 4 -,-CH 2 NHCOCH 2
-, - CH 2 NHCO (CH 2) 4 -, - SO 2 NHCH 2 -, - SO 2 NH (CH 2) 4 - , and the like. The group X represents a bromine atom and / or a chlorine atom, and the total number of these substituents is 0-12. 0
When it is mixed with green highly halogenated copper phthalocyanine, the amount thereof is preferably reduced. In general, the halogenated copper phthalocyanine having a total number of 11 to 12 has severe manufacturing conditions and is likely to generate a by-product. Therefore, the halogenated copper phthalocyanine having a total number of 5 to 10 is converted into a green highly halogenated copper phthalocyanine. Mixing is practically advantageous. Also, with the same number of substituents, the bromine-substituted derivative becomes yellowish green compared to chlorine. It should be noted that the number of substituents in the synthesized copper phthalocyanine derivative is an average number of those, since some of them are generally mixed when actually measured.

一般式〔I〕の銅フタロシアニン誘導体と銅フタロシア
ニンまたはハロゲン化銅フタロシアニンとの混合は、乾
燥粉末,プレスケーキまたはスラリーの状態で行うこと
が出来,また両者を別々にあるいは共に濃硫酸に溶解ま
たは懸濁し、水に注入することによって顔料を析出さ
せ,あるいは粗製銅フタロシアニンまたは粗製高ハロゲ
ン化銅フタロシアニンと共に機械的に摩砕することによ
って顔料化と混合を同時に行うことも出来る。また,銅
フタロシアニンまたはハロゲン化銅フタロシアニンと銅
フタロシアニン誘導体とを別々に準備し,樹脂の着色成
形等の時に添加することも可能である。さらには混合し
た銅フタロシアニンまたはハロゲン化銅フタロシアニン
顔料組成物は,ポリエステル樹脂の作業性および分散状
態を良くするために従来から知られているドライカラ
ー,ペーストカラー,リキッドカラーまたはマスターバ
ッチのような加工顔料とすることが有利である。
The copper phthalocyanine derivative of the general formula [I] and the copper phthalocyanine or the halogenated copper phthalocyanine can be mixed in the form of a dry powder, a press cake or a slurry, and both of them can be dissolved or suspended in concentrated sulfuric acid separately or together. Pigmentation and mixing can also be carried out simultaneously by making the pigment cloudy and pouring it into water, or mechanically milling with crude copper phthalocyanine or crude highly halogenated copper phthalocyanine. It is also possible to separately prepare copper phthalocyanine or a halogenated copper phthalocyanine and a copper phthalocyanine derivative and add them at the time of coloring and molding the resin. In addition, the mixed copper phthalocyanine or halogenated copper phthalocyanine pigment composition may be processed by dry color, paste color, liquid color or masterbatch processing conventionally known to improve the workability and dispersion of the polyester resin. Advantageously, it is a pigment.

銅フタロシアニンまたはハロゲン化銅フタロシアニン組
成物について,銅フタロシアニンまたはハロゲン化銅フ
タロシアニン100重量部に対して前記一般式〔I〕で
示される銅フタロシアニン誘導体を0.5〜30重量部混
合するか,0.5重量部未満では顔料粒子の集合および結
晶の成長,転移を抑制するための効果を示さず,一方3
0重量部を超えて混合した場合には耐溶剤性および色相
が不鮮明になるなどの問題を生ずるため,0.5〜30重
量部,好ましくは5〜15重量部を混合する。
Regarding the copper phthalocyanine or halogenated copper phthalocyanine composition, 0.5 to 30 parts by weight or less than 0.5 parts by weight of the copper phthalocyanine derivative represented by the general formula [I] is mixed with 100 parts by weight of copper phthalocyanine or halogenated copper phthalocyanine. Does not show the effect of suppressing the aggregation of pigment particles and the growth and transition of crystals.
When the amount is more than 0 parts by weight, problems such as solvent resistance and unclear hue occur, so 0.5 to 30 parts by weight, preferably 5 to 15 parts by weight is mixed.

本発明において、非結晶性および非集合性に優れている
理由が必ずしも明らかではないが,一般式〔I〕で示さ
れる銅フタロシアニン誘導体は化学構造からも明らかな
ようにアルキル基などが結合していることにより塩基性
が高められた第3級アミノ基を有していることに起因
し,これより被分散体であるポリエステル樹脂との相互
作用が生じているものと推定できる。
In the present invention, the reason why it is excellent in non-crystallinity and non-aggregation property is not necessarily clear, but the copper phthalocyanine derivative represented by the general formula [I] has an alkyl group or the like bonded to it, as is clear from the chemical structure. It is presumed that the presence of a tertiary amino group having an increased basicity as a result of the presence thereof causes an interaction with the polyester resin that is the substance to be dispersed.

本発明者などの実験によると,下記一般式〔II〕 〔X〕−CuPc−〔A−NHR (ただし式〔II〕のCuPc,X,A,m,nおよびR1は式〔I〕と
同じ)で表される第2級アミノ基を有する銅フタロシア
ニン誘導体のポリエステル樹脂への添加では,結晶性お
よび集合性の改良には不十分であった。
According to experiments by the present inventors, the following general formula [II] [X] m -CuPc- [A-NHR 1 ] n (where CuPc, X, A, m, n and R 1 in the formula [II] are represented by the formula The addition of a copper phthalocyanine derivative having a secondary amino group represented by the same formula (I)) to the polyester resin was insufficient for improving the crystallinity and the aggregation property.

以下,実施例により本発明を説明する。例中,部とは重
量部,%とは重量%をそれぞれ表す。
The present invention will be described below with reference to examples. In the examples, "part" means "part by weight" and "%" means "% by weight".

製造例1 ビス−(クロルメチル)銅フタロシアニン10部を含む
水スラリーにジエチルアミン5部を加え,70℃で5時
間攪拌し,顔料色素を濾別し,水で洗い乾燥して下記に
示す銅フタロシアニン誘導体を得た。
Production Example 1 5 parts of diethylamine was added to a water slurry containing 10 parts of bis- (chloromethyl) copper phthalocyanine, and the mixture was stirred at 70 ° C. for 5 hours, the pigment dye was filtered off, washed with water and dried to give the copper phthalocyanine derivative shown below. Got

製造例2 ビス−(クロルメチル)−オクタクロル銅フタロシアニ
ン10部を含む水スラリーにピペリジン4部を加え,1
00℃で4時間攪拌し,顔料色素を濾別し,水で洗い乾
燥して下記に示す銅フタロシアニン誘導体を得た。
Production Example 2 4 parts of piperidine was added to an aqueous slurry containing 10 parts of bis- (chloromethyl) -octachlorocopper phthalocyanine, and 1
The mixture was stirred at 00 ° C. for 4 hours, the pigment dye was filtered off, washed with water and dried to obtain a copper phthalocyanine derivative shown below.

製造例3〜9 各種銅フタロシアニン誘導体を上記製造例に準じて製造
し,表−1に示す。
Production Examples 3 to 9 Various copper phthalocyanine derivatives were produced according to the above production examples and shown in Table 1.

実施例1〜9 表−1に示した組成の銅フタロシアニン組成物を用いて
下記に示す配合割合で不飽和ポリエステル樹脂および溶
融紡糸用着色剤を作成した。
Examples 1 to 9 Using the copper phthalocyanine composition having the composition shown in Table 1, unsaturated polyester resins and melt-spinning colorants were prepared at the following compounding ratios.

〔成形用不飽和ポリエステル樹脂用着色剤〕[Colorant for unsaturated polyester resin for molding]

銅フタロシアニン顔料組成物10部,酸化チタン50部
および不飽和ポリエステル樹脂(無水マレンン酸,無水
フタル酸およびジエチレングリコールにより得られた)
40部を3本ロールミルで混練して本発明の着色剤1−
(I)〜9−(I)を得た。
Copper phthalocyanine pigment composition 10 parts, titanium oxide 50 parts and unsaturated polyester resin (obtained with maleic anhydride, phthalic anhydride and diethylene glycol)
Coloring agent of the present invention 1-
(I) to 9- (I) were obtained.

〔溶融紡糸用着色剤〕[Coloring agent for melt spinning]

液状ポリエステル樹脂(アジピン酸および1,3−ブチ
レングリコールとからなる液状ポリエステル(商品名ア
デカサイザーP−300,アデカ・アーガス化学製))
70部と銅フタロシアニン顔料組成物30部を三本ロー
ルで混練して,本発明の着色剤1−(II)〜9−(II)
を得た。
Liquid polyester resin (liquid polyester consisting of adipic acid and 1,3-butylene glycol (trade name: ADEKA SAIZER P-300, manufactured by ADEKA ARGUS CHEMICAL))
70 parts and 30 parts of the copper phthalocyanine pigment composition were kneaded with a three-roll mill to form the colorants 1- (II) to 9- (II) of the present invention.
Got

〔成形用不飽和ポリエステル樹脂の着色1−(I)〜9
−(I)〕 下記組成の成形用不飽和ポリエステル樹脂組成物100
部に本発明の着色剤1−(I)〜9−(I)をそれぞれ
5部加え,シートモールディングコンパウンドを調整
し,ガラス繊維へ十分含浸させ,ポリエチレンフィルム
で覆い,40℃で2日間熟成させ,次いで金型(サイズ
−縦15cm,横15cm,厚さ0.8cm)で140℃,3分
間,プレス圧100Kg/cm2の条件で着色成形した。得ら
れた着色成形物の着色むら,着色力および色相の変化を
調べた結果,着色成形物は均一に着色されており,着色
力の低下および色相の変化は認められなかった。また,
成形物の機械的強度または耐薬品性などの低下は全く認
められず良好であった。
[Coloring of unsaturated polyester resin for molding 1- (I) to 9
-(I)] An unsaturated polyester resin composition for molding 100 having the following composition
5 parts of each of the colorants 1- (I) to 9- (I) of the present invention was added to each part to adjust the sheet molding compound, and the glass fibers were sufficiently impregnated, covered with a polyethylene film, and aged at 40 ° C. for 2 days. Then, it was colored and molded in a mold (size-15 cm in length, 15 cm in width, 0.8 cm in thickness) at 140 ° C. for 3 minutes under a press pressure of 100 kg / cm 2 . As a result of examining the coloring unevenness, the coloring power and the change in hue of the obtained colored molded product, it was found that the colored molded product was uniformly colored, and the decrease in the coloring power and the change in hue were not observed. Also,
The molded product was good, with no deterioration in mechanical strength or chemical resistance.

(成形用不飽和ポリエステル樹脂組成物) 熱硬化型不飽和ポリエステル樹脂 ポリマール9607(武田薬品工業(株)) 50部 ポリマール6819(武田薬品工業(株)) 20部 炭酸カルシウム(日東粉化(株)) 100部 ステアリン酸亜鉛 2部 酸化マグネシウム 1部 t−ブチルパーオキシベンゾエート 1部 低収縮性付与剤(ポリマール9965) 30部 ポリエチレン粉(フローセンUF−80, 製鉄化学(株)) 5部 以上の組成に対し25重量%のガラス繊維を用いる。(Unsaturated Polyester Resin Composition for Molding) Thermosetting unsaturated polyester resin Polymer 9607 (Takeda Pharmaceutical Co., Ltd.) 50 parts Polymer 6819 (Takeda Pharmaceutical Co., Ltd.) 20 parts Calcium carbonate (Nitto Powder Co., Ltd.) ) 100 parts Zinc stearate 2 parts Magnesium oxide 1 part t-Butyl peroxybenzoate 1 part Low shrinkage imparting agent (Polymer 9965) 30 parts Polyethylene powder (FLOWSEN UF-80, Iron and Chemicals Co., Ltd.) 5 parts or more composition To 25% by weight of glass fiber.

〔飽和ポリエステル樹脂の着色1−(II)〜9−(I
I)〕 極限粘度値(IV値)0.70のポリエチレンテレフタレー
ト樹脂(商品名ベルベットEFG−6,カネボウ合繊
製)100部に本発明の着色剤1−(II)〜9−(II)
を3部を定量供給し,40μ5層フィルターを有する紡
糸機にて290℃で紡糸を行った。
[Coloring of saturated polyester resin 1- (II) to 9- (I
I)] 100 parts of polyethylene terephthalate resin having an intrinsic viscosity value (IV value) of 0.70 (trade name: Velvet EFG-6, manufactured by Kanebo Gosei Co., Ltd.) is added to 100 parts of the colorant 1- (II) to 9- (II) of the present invention.
Was quantitatively supplied, and spinning was carried out at 290 ° C. with a spinning machine having a 40 μ5 layer filter.

得られた繊維をミクロトーム(PR50型回転式,大和
光機工業(株))でカットし、顕微鏡を用いて10μ以
上の凝集物を測定した結果,全く認められず,また3日
間の操業でのフィルター圧の上昇および耐糸切れ性も良
好であった。
The obtained fiber was cut with a microtome (PR50 type rotary type, Yamato Koki Kogyo Co., Ltd.), and the result of measuring agglomerates of 10 μ or more using a microscope showed that no agglomerates were observed at all, and after 3 days of operation The rise in filter pressure and the yarn breakage resistance were also good.

さらに本発明の着色剤1−(II)〜9−(II)の添加量
を7部まで増したが,顕微鏡での凝集物および操業性は
良好であった。
Further, the addition amount of the colorants 1- (II) to 9- (II) of the present invention was increased to 7 parts, but the agglomerates and the workability under a microscope were good.

以上の結果を表−2に示す。The above results are shown in Table 2.

比較例1〜6 下記表−3に示す銅フタロシアニンまたはハロゲン化銅
フタロシアニン顔料を用いて実施例と同様な操作を行っ
たところ,成形用不飽和ポリエステル樹脂の着色におい
ては,着色不均一,かつ着色力不足であり,飽和ポリエ
ステル樹脂の着色においても凝集物が多く,フィルター
での圧上昇も高く(表−4参照),本発明の実施例であ
る1−(I)〜9−(I)および1−(II)〜9−(I
I)に比べ明らかに不良であった。
Comparative Examples 1 to 6 When copper phthalocyanine or halogenated copper phthalocyanine pigments shown in Table 3 below were used and the same operation as in Example was carried out, the unsaturated polyester resin for molding was colored unevenly and colored. Insufficient power, a large amount of aggregates in coloring the saturated polyester resin, and a high pressure increase in the filter (see Table 4), which are Examples of the present invention 1- (I) to 9- (I) and 1- (II) -9- (I
It was clearly worse than I).

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭52−111926(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-52-111926 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ポリエステル樹脂を着色するに際して、銅
フタロシアニンおよびもしくはハロゲン化銅フタロシア
ニン100重量部および下記一般式〔I〕で示される銅
フタロシアニン誘導体0.5〜30重量部を用いること
を特徴とする着色方法。 一般式〔I〕 (式中、CuPcは銅フタロシアニン残基、Xはハロゲ
ン原子、Aは基−(CH−,−CHNH(CH
−,−CHNHCO(CH −,−SO
NH(CH −を表し(ただし、R,Rはアル
キル基またはRとRとで少なくとも窒素原子を含む
6員環を示す。)、mは0〜10、nは1〜8、kは1
〜2、は1〜4の整数を表す。)
1. When coloring a polyester resin, copper is used.
Phthalocyanine and / or copper halide phthalocyanine
100 parts by weight of nin and copper represented by the following general formula [I]
Use 0.5 to 30 parts by weight of phthalocyanine derivative
And a coloring method. General formula [I](In the formula, CuPc is a copper phthalocyanine residue, and X is a halogen.
Atom, A is a group-(CHTwo)k-,-CHTwoNH (CH
Two) -,-CHTwoNHCO (CHTwo) -,-SOTwo
NH (CHTwo) Represents − (where R1, RTwoIs al
Kill group or R1And RTwoAnd contains at least a nitrogen atom
Indicates a 6-membered ring. ), M is 0-10, n is 1-8, k is 1
~ 2 represents an integer of 1 to 4. )
JP60270655A 1985-12-03 1985-12-03 Method for coloring polyester resin Expired - Lifetime JPH0625295B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60270655A JPH0625295B2 (en) 1985-12-03 1985-12-03 Method for coloring polyester resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60270655A JPH0625295B2 (en) 1985-12-03 1985-12-03 Method for coloring polyester resin

Publications (2)

Publication Number Publication Date
JPS62131054A JPS62131054A (en) 1987-06-13
JPH0625295B2 true JPH0625295B2 (en) 1994-04-06

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ID=17489111

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Application Number Title Priority Date Filing Date
JP60270655A Expired - Lifetime JPH0625295B2 (en) 1985-12-03 1985-12-03 Method for coloring polyester resin

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Country Link
JP (1) JPH0625295B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3813750B2 (en) * 1998-08-27 2006-08-23 大日精化工業株式会社 Color filter manufacturing method and color filter
US7077896B2 (en) * 2003-06-13 2006-07-18 Toyo Ink Mfg. Co., Ltd. Pigment composition and use thereof in plastic
JP4525191B2 (en) * 2003-06-13 2010-08-18 東洋インキ製造株式会社 Pigment compositions and their use in plastics
JP7151091B2 (en) * 2017-02-15 2022-10-12 東洋インキScホールディングス株式会社 colored resin composition

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52111926A (en) * 1976-03-17 1977-09-20 Dainichi Seika Kogyo Kk Coloring agent for polyester polymer

Also Published As

Publication number Publication date
JPS62131054A (en) 1987-06-13

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