JPS62131072A - Production of copper phthalocyanine pigment - Google Patents

Production of copper phthalocyanine pigment

Info

Publication number
JPS62131072A
JPS62131072A JP26948785A JP26948785A JPS62131072A JP S62131072 A JPS62131072 A JP S62131072A JP 26948785 A JP26948785 A JP 26948785A JP 26948785 A JP26948785 A JP 26948785A JP S62131072 A JPS62131072 A JP S62131072A
Authority
JP
Japan
Prior art keywords
copper phthalocyanine
pigment
water
butyl cellosolve
crude copper
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.)
Pending
Application number
JP26948785A
Other languages
Japanese (ja)
Inventor
Akira Mori
毛利 亮
Seizo Kibe
木部 誠三
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.)
Dainichiseika Color and Chemicals Mfg Co Ltd
Original Assignee
Dainichiseika Color and Chemicals 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 Dainichiseika Color and Chemicals Mfg Co Ltd filed Critical Dainichiseika Color and Chemicals Mfg Co Ltd
Priority to JP26948785A priority Critical patent/JPS62131072A/en
Publication of JPS62131072A publication Critical patent/JPS62131072A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain copper phthalocyanine pigment having a high color density, by mixing dried, ground crude copper phthalocyanine with an aq. soln. of butyl cellosolve at room temp. and heating the mixture at a specified temp. CONSTITUTION:Crude copper phthalocyanine is dried and ground. The resulting ground material is blended with an aq. soln. of 9-58% butyl cellosolve in a ratio of the ground material to butyl cellosolve of 1:1-0.05. The mixture is homogeneously mixed at room temp. and then heated at 50-100 deg.C to obtain the desired pigment. Examples of grinding aids for use in grinding crude copper phthalocyanine are water-soluble materials such as sodium chloride, sodium sulfate and calcium chloride. Butyl cellosolve is soluble in water at room temp. and well dissolved in water. However, when it is heated to 50 deg.C or above, it becomes water-insoluble. Thus, when butyl cellosolve is mixed with water and the pigment is treated at 50 deg.C or above, butyl cellosolve is separated from water, completely absorbed by the surface of the pigment and effectively promotes the crystal transition and the crystallization of the pigment.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、塗料、印刷インキ、プラスチック用着色剤等
に有用な色濃度の高い顔料形態を有する銅フタロシアニ
ン顔料の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a copper phthalocyanine pigment having a pigment form with high color density useful for paints, printing inks, colorants for plastics, and the like.

〔従来技術〕[Prior art]

通常の合成反応によって得られた粗製銅フタロシアニン
は、着色力及び色相等において顔料特性に欠けている。
Crude copper phthalocyanine obtained through ordinary synthetic reactions lacks pigmentary properties in terms of coloring power, hue, and the like.

そのため粗製の銅フタロシアニンを有用な顔料形態に転
化させるために種々の方法が行われいてる。
Therefore, various methods have been used to convert crude copper phthalocyanine into useful pigment forms.

例えば、粗製銅フタロシアニンに摩砕助剤を加えてボー
ルミル等で乾式摩砕を行なう方法がある。
For example, there is a method in which a grinding aid is added to crude copper phthalocyanine and dry grinding is performed using a ball mill or the like.

そして顔料化に際しては、この摩砕顔料に対して当量以
上の有機溶媒(アルコール類、キジロール類等)中で顔
料化しているのが一般的である。
When turning into a pigment, the ground pigment is generally turned into a pigment in an amount of organic solvent (alcohols, pheasants, etc.) equal to or more than that of the ground pigment.

好ましくは3〜lO倍量の溶媒中で攪拌ないしは加熱攪
拌し、1〜4時間で顔料化し鮮明なβ型銅フタロシアニ
ンブルー顔料が得られている。
Preferably, it is stirred or heated and stirred in a solvent of 3 to 10 times the amount, and is converted into a pigment in 1 to 4 hours to obtain a clear β-type copper phthalocyanine blue pigment.

〔発明が解決しようとしている問題点〕上記の乾式摩砕
法によると多量の有機溶媒を使用しなければならない。
[Problems to be Solved by the Invention] According to the above dry milling method, a large amount of organic solvent must be used.

従来使用している溶媒例えばブタノール、キジロールで
は、溶媒量を顔料に対して当量以上加えないと顔料化が
十分行なわれず、そのため、多量の溶媒を用いるので、
作業環境がよくなく、危険性を供ない、溶媒回収の問題
等大きな課題であった。
Conventionally used solvents, such as butanol and quijirol, cannot be sufficiently pigmented unless an equivalent amount or more is added to the pigment, so a large amount of solvent is used.
The work environment was not good, it was dangerous, and problems with solvent recovery were major issues.

本発明者らは、これら従来法の欠陥を改善すべく鋭意研
究を重ねた結果、有機溶媒として特にブチルセロソルブ
を採択して使用した結果、顔料に対する溶媒の使用量が
当量以下でも十分に顔料化が行なえて、高鮮明なβ型銅
フタロシアニンブルーが得られることを知見して本発明
に到達した。
As a result of intensive research to improve the deficiencies of these conventional methods, the present inventors specifically adopted butyl cellosolve as an organic solvent. The present invention was achieved based on the finding that highly clear β-type copper phthalocyanine blue can be obtained by carrying out this process.

〔問題を解決するための手段〕[Means to solve the problem]

すなわち、本発明は、 粗製銅フタロシアニンを乾燥摩砕し、得られた摩砕物に
対して、9〜58%のブチルセロソルブ水溶液を前記摩
砕物に対してブチルセロソルブ量換算で1=1〜0.0
5となるように配合し、常温で均一に混合した後、更に
50〜100℃で加熱処理することを特徴とする銅フタ
ロシアニン顔料の製造方法である。
That is, in the present invention, crude copper phthalocyanine is dry-milled, and a 9 to 58% butyl cellosolve aqueous solution is added to the ground product in an amount of 1 = 1 to 0.0 in terms of the amount of butyl cellosolve to the ground product.
5, uniformly mixed at room temperature, and then further heat-treated at 50 to 100°C.

本発明を更に詳細に説明する。The present invention will be explained in more detail.

本発明で用いられる粗製銅フタロシアニンとしては、従
来公知の方法で得られる銅フタロシアニン、分子中に2
個以下の塩素原子もしくは臭素原子を含有する銅フタロ
シアニン、ポリクロル銅フタロシアニン、分子中に14
個以下の臭素原子を含をするポリクロルーブロム銅フタ
ロシアニン等が挙げられる。
The crude copper phthalocyanine used in the present invention includes copper phthalocyanine obtained by a conventionally known method,
Copper phthalocyanine, polychlorocopper phthalocyanine containing up to 14 chlorine or bromine atoms in the molecule
Examples include polychloro-bromine copper phthalocyanine containing up to 3 bromine atoms.

前記の粗製銅フタロシアニンを摩砕するために用いる摩
砕助剤としては、塩化ナトリウム、硫酸ナトリウムおよ
び塩化カルシウムなどの水溶性のものがあげられ、これ
らは一種又は二種以上混合して使用される。
As the grinding aid used for grinding the above-mentioned crude copper phthalocyanine, water-soluble ones such as sodium chloride, sodium sulfate and calcium chloride can be mentioned, and these can be used singly or in combination of two or more. .

摩砕助剤の使用量は粗製銅フタロシアニンに対し2〜1
0重量倍、好ましくは5〜7重量倍である。
The amount of grinding aid used is 2 to 1 per crude copper phthalocyanine.
0 times by weight, preferably 5 to 7 times by weight.

本発明では、乾式摩砕した粗製銅フタロシアニンにブチ
ルセロソルブを加えて溶剤処理することを特徴とするも
のであるが、前記のブチルセロソルブは水と併用される
が、ブチルセロソルブの使用量は、粗製銅フタロシアニ
ンに対して5〜100重量%、好ましくは20〜40重
量%である。
The present invention is characterized by adding butyl cellosolve to dry-milled crude copper phthalocyanine and treating it with a solvent. The above-mentioned butyl cellosolve is used in combination with water, but the amount of butyl cellosolve used is the same as that of the crude copper phthalocyanine. The amount is 5 to 100% by weight, preferably 20 to 40% by weight.

ブチルセロソルブの使用に際しては、まず水とブチルセ
ロソルブを混合し、この混合物を顔料摩砕物に加えて混
合、5〜100℃で加熱処理を行なう。
When using butyl cellosolve, first, water and butyl cellosolve are mixed, and this mixture is added to the ground pigment, mixed, and heat-treated at 5 to 100°C.

摩砕、ブチルセロソルブ処理後の銅フタロシアニン顔料
の取出に際して、ブチルセロソルブを除去するに当って
は、50℃以下の洗浄水で洗うとブチルセロソルブは水
溶性となるため顔料から容易に除去することができる。
When removing the copper phthalocyanine pigment after grinding and butyl cellosolve treatment, butyl cellosolve can be easily removed from the pigment by washing with washing water at 50° C. or lower, as the butyl cellosolve becomes water-soluble.

ブチルセロソルブは常温では水溶性であり、水とよく混
ざるが50℃以上に加熱した場合、水に不溶性となる。
Butyl cellosolve is water-soluble at room temperature and mixes well with water, but when heated to 50°C or higher, it becomes insoluble in water.

従ってブチルセロソルブを水と混合して50℃以上で顔
料を処理すると、ブチルセロソルブは水と分離して完全
に顔料表面に吸着し、効率よく、顔料の結晶転移と、結
晶化を推進する働きをなす。
Therefore, when butyl cellosolve is mixed with water and the pigment is treated at 50°C or higher, butyl cellosolve is separated from the water and completely adsorbed on the pigment surface, efficiently promoting the crystal transition and crystallization of the pigment.

以下、実施例により本発明を具体的に説明する。Hereinafter, the present invention will be specifically explained with reference to Examples.

実施例1゜ 乾式アトライク−に粗製の銅フタロシアニン100重量
部を加え30分間粉砕する。
Example 1 100 parts by weight of crude copper phthalocyanine was added to a dry attrike and pulverized for 30 minutes.

この粉砕した粗製銅フタロシアニンについてX線回折で
β型結晶形の含有率を調べた結果43%であった0 次いで得られた摩砕物100重量部にブチルセロソルブ
30重量部、水200重量部を加え、常温で30分間混
合を行なう。更に内容物を90°Cに加熱し、4時間攪
拌混合を行なう。次いで、混合物を大量の水中に投入し
、2%希硫酸水溶液で80℃〜90℃、50分間加熱処
理を行なう。
The content of the β-type crystal form of this crushed crude copper phthalocyanine was examined by X-ray diffraction, and the result was 43%.Next, 30 parts by weight of butyl cellosolve and 200 parts by weight of water were added to 100 parts by weight of the obtained crushed product. Mix for 30 minutes at room temperature. Further, the contents were heated to 90°C and stirred and mixed for 4 hours. Next, the mixture is poured into a large amount of water and heat-treated with a 2% dilute sulfuric acid aqueous solution at 80° C. to 90° C. for 50 minutes.

次に濾過、水洗し、得られた顔料ケーキを70〜80℃
で乾燥する。鮮明なβ型銅フタロシアニン顔料が得られ
た。
Next, filter, wash with water, and store the resulting pigment cake at 70-80°C.
Dry with. A clear β-type copper phthalocyanine pigment was obtained.

実施例2゜ 乾式アトライターに粗製の銅フタロシアニン100重量
部を加え30分間粉砕する。
Example 2 100 parts by weight of crude copper phthalocyanine was added to a dry attritor and ground for 30 minutes.

この粉砕した粗製銅フタロシアニンについてX線回折で
β型結晶形の含有率を調べた結果43%であった。
The content of β-type crystals in this pulverized crude copper phthalocyanine was examined by X-ray diffraction and was found to be 43%.

次いで得られた摩砕物100重量部にブチルセロソルブ
30重量部、40%硫酸水溶液200!It量部を加え
、常温で30分間混合を行なう。更に内容物を90″C
に加熱し、4時間攪拌混合を行なう。
Next, to 100 parts by weight of the obtained ground material, 30 parts by weight of butyl cellosolve and 200 parts by weight of a 40% aqueous sulfuric acid solution! Add 1 part of It and mix for 30 minutes at room temperature. Furthermore, the contents were heated to 90″C.
and stir and mix for 4 hours.

次いで混合物を大量の水中に投入し、更に濾過、水洗し
、得られた顔料ケーキを70〜80°Cで乾燥する。鮮
明なβ型銅フタロシアニン顔料が得られた。
The mixture is then poured into a large amount of water, further filtered and washed with water, and the resulting pigment cake is dried at 70-80°C. A clear β-type copper phthalocyanine pigment was obtained.

実施例3゜ 乾式アトライターに粗製の銅フタロシアニン100重量
部を加え30分間粉砕する。
Example 3 100 parts by weight of crude copper phthalocyanine was added to a dry attritor and pulverized for 30 minutes.

この粉砕した粗製銅フタロシアニンについてX線回折で
β型結晶形の含有率を調べた結果43%であった。
The content of β-type crystals in this pulverized crude copper phthalocyanine was examined by X-ray diffraction and was found to be 43%.

次いで得られた摩砕物100重量部に6%水酸化ナトリ
ウム溶液200重量部を加え、常温で30分間混合を行
なう。更に内容物を80〜90℃に加熱し、3〜4時間
撹拌混合を行なう。
Next, 200 parts by weight of a 6% sodium hydroxide solution was added to 100 parts by weight of the obtained ground material, and the mixture was mixed for 30 minutes at room temperature. Further, the contents are heated to 80 to 90°C and stirred and mixed for 3 to 4 hours.

次いで混合物を大量の水中に投入し、更に濾過、水洗し
、得られた顔料ケーキを70〜80℃で乾燥する。鮮明
なβ型銅フタロシアニン顔料が得られた。
The mixture is then poured into a large amount of water, further filtered and washed with water, and the resulting pigment cake is dried at 70-80°C. A clear β-type copper phthalocyanine pigment was obtained.

比較例1゜ 乾式アトライターに粗製の銅フタロシアニン100重量
部を加え30分間粉砕する。
Comparative Example 1 100 parts by weight of crude copper phthalocyanine was added to a dry attritor and pulverized for 30 minutes.

この粉砕した粗製銅フタロシアニンについてX線回折で
β型結晶形の含有率を調べた結果43%であった。
The content of β-type crystals in this pulverized crude copper phthalocyanine was examined by X-ray diffraction and was found to be 43%.

次いで得られた摩砕物100重量部にイソプロピルアル
コール200重量部、水200重量部を加え、内容物を
79.5℃に加熱し、4時間撹拌混合を行なう。
Next, 200 parts by weight of isopropyl alcohol and 200 parts by weight of water were added to 100 parts by weight of the obtained ground material, and the contents were heated to 79.5°C and stirred and mixed for 4 hours.

次いで混合物を大量の水中に投入し、2%希硫酸水溶液
で80℃〜90℃、50分間加熱処理を行なう。次に濾
過、水洗し、得られた顔料ケーキを70〜80℃で乾燥
する。得られたβ型銅フタロシアニン顔料は、実施例1
で得たβ型銅フタロシアニン顔料と比較して着色力がな
く、色調が不鮮明であった。
Next, the mixture is poured into a large amount of water and heat-treated with a 2% dilute sulfuric acid aqueous solution at 80°C to 90°C for 50 minutes. Next, it is filtered and washed with water, and the resulting pigment cake is dried at 70 to 80°C. The obtained β-type copper phthalocyanine pigment was prepared in Example 1.
Compared to the β-type copper phthalocyanine pigment obtained in Example 1, the pigment had no coloring power and the color tone was unclear.

〔作用効果〕[Effect]

本発明では、乾式摩砕した粗製銅フタロシアニン顔料を
ブチルセロソルブと水の混合物で50〜100℃で加熱
処理する結果、該ブチルセロソルブは水と分離して完全
に顔料表面に吸着し、効率よく顔料の結晶転移と結晶を
促進するため、従来法と比較し、溶媒の使用が極めて少
なくて済み、溶剤による作業環境汚染や危険性の心配が
ない。
In the present invention, dry-milled crude copper phthalocyanine pigment is heat-treated with a mixture of butyl cellosolve and water at 50 to 100°C. As a result, the butyl cellosolve is separated from water and completely adsorbed on the pigment surface, resulting in efficient pigment crystallization. Because it promotes transition and crystallization, it requires significantly less solvent than conventional methods, and there is no need to worry about contaminating the working environment or being dangerous.

また溶媒の回収に手間を要することなく経済的にもすぐ
れた製造法である。
Moreover, it is an economically superior manufacturing method as it does not require much effort to recover the solvent.

更にまた強酸性〜中性〜強アルカリ性の水溶液下で実施
しても、それぞれ特徴ある色相を有する鮮明、着色力の
ある銅フタロシアニン顔料が得られる。
Furthermore, even when the process is carried out under strongly acidic to neutral to strongly alkaline aqueous solutions, copper phthalocyanine pigments with distinct hues and vivid coloring powers can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 粗製銅フタロシアニンを乾燥摩砕し、得られた摩砕物に
対して、9〜58%のブチルセロソルブ水溶液を前記摩
砕物に対してブチルセロソルブ量換算で1:1〜0.0
5となるように配合し、常温で均一に混合した後、更に
50〜100℃で加熱処理することを特徴とする銅フタ
ロシアニン顔料の製造方法。
Crude copper phthalocyanine is dry-milled, and a 9 to 58% butyl cellosolve aqueous solution is added to the ground product at a ratio of 1:1 to 0.0 in terms of the amount of butyl cellosolve to the ground product.
A method for producing a copper phthalocyanine pigment, which comprises mixing the pigments uniformly at room temperature and then heat-treating the pigments at 50 to 100°C.
JP26948785A 1985-12-02 1985-12-02 Production of copper phthalocyanine pigment Pending JPS62131072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26948785A JPS62131072A (en) 1985-12-02 1985-12-02 Production of copper phthalocyanine pigment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26948785A JPS62131072A (en) 1985-12-02 1985-12-02 Production of copper phthalocyanine pigment

Publications (1)

Publication Number Publication Date
JPS62131072A true JPS62131072A (en) 1987-06-13

Family

ID=17473123

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26948785A Pending JPS62131072A (en) 1985-12-02 1985-12-02 Production of copper phthalocyanine pigment

Country Status (1)

Country Link
JP (1) JPS62131072A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0685533A1 (en) 1994-06-03 1995-12-06 Toyo Ink Manufacturing Co., Ltd. Method of adjusting pigment particles, pigment and colorant composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5575453A (en) * 1978-11-30 1980-06-06 Basf Ag Manufacture of readily dispersible and deep color pigment state

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5575453A (en) * 1978-11-30 1980-06-06 Basf Ag Manufacture of readily dispersible and deep color pigment state

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0685533A1 (en) 1994-06-03 1995-12-06 Toyo Ink Manufacturing Co., Ltd. Method of adjusting pigment particles, pigment and colorant composition

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