JPS63207858A - Production of copper phthalocyanine pigment - Google Patents

Production of copper phthalocyanine pigment

Info

Publication number
JPS63207858A
JPS63207858A JP4222187A JP4222187A JPS63207858A JP S63207858 A JPS63207858 A JP S63207858A JP 4222187 A JP4222187 A JP 4222187A JP 4222187 A JP4222187 A JP 4222187A JP S63207858 A JPS63207858 A JP S63207858A
Authority
JP
Japan
Prior art keywords
parts
copper phthalocyanine
copper
compound
formula
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
JP4222187A
Other languages
Japanese (ja)
Inventor
Taira Fujita
藤田 平
Noriaki Kishimoto
憲明 岸本
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP4222187A priority Critical patent/JPS63207858A/en
Priority to US07/110,528 priority patent/US4785091A/en
Priority to DE8787309637T priority patent/DE3787072D1/en
Priority to EP87309637A priority patent/EP0266219B1/en
Publication of JPS63207858A publication Critical patent/JPS63207858A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To directly produce the titled pigment only by a synthetic reaction without using pigmentation process, by adding a specific component in addition to a catalyst to a reaction system in the synthesis of copper phthalocyanine from phthalic acid, copper, etc., in an organic solvent. CONSTITUTION:The objective pigment is produced by reacting phthalic acid and/or its derivative with urea and copper (compound) in an organic solvent (e.g. nitrobenzene) in he presence of a catalyst (e.g. titanium tetrachloride) and a compound of formula (A and B are H, alkyl, allyl, etc.) usually at 150-250 deg.C. The compound of formula is e.g. pyromellitic acid anhydride diimide. The amount of the compound of formula I is usually 1-30wt.% based on the phthalic acid, etc.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、色相鮮明で着色力も大きく優れた青色顔料と
して、インキ、塗料、プラスチック等の着色剤として広
く使用されてい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 is directed to the production of a copper phthalocyanine pigment, which is widely used as a coloring agent for inks, paints, plastics, etc. as a blue pigment with a clear hue and great coloring power. It is about the method.

〈従来の技術〉 銅フタロシアニン顔料は、次の如き粗製銅フタロシアニ
ンの合成工程と粗製銅フタロシアニンを微粒化する顔料
化工程を経て製造されるのが一般的である。
<Prior Art> Copper phthalocyanine pigments are generally produced through the following steps of synthesizing crude copper phthalocyanine and turning the crude copper phthalocyanine into fine particles.

(1)合成工程 無水フタル酸若しくはその誘導体、銅若しくはその化合
物、尿素等の窒素源及び少量の触媒を不活性な高沸点溶
剤中で加熱することにより粗製銅フタロシアニンを得る
(1) Synthesis Step Crude copper phthalocyanine is obtained by heating phthalic anhydride or its derivatives, copper or its compound, a nitrogen source such as urea, and a small amount of catalyst in an inert high-boiling solvent.

(2)顔料化工程 上記合成工程によって得られた銅フタロシアニンは粗大
粒子の塊状物であるため、色調が不鮮明で着色力が乏し
く、このままの状態では実用に供し得ない。従って、着
色力、鮮明度及び顔料適性を付与するために顔料化工程
が必要となる。この工程は、主に硫酸を用いて、硫酸と
塩を形成させるか又は高濃度の硫酸に溶解させたものを
多量の水に注ぎ微粒子を得る化学的微粒子化法とボール
ミルやニーダ−等を用いる機械的摩砕による物理的微粒
子化法がある。
(2) Pigment formation step Since the copper phthalocyanine obtained by the above synthesis step is a lump of coarse particles, the color tone is unclear and the coloring power is poor, and it cannot be put to practical use in this state. Therefore, a pigmentation step is required to impart tinting strength, sharpness and pigment suitability. This process mainly uses sulfuric acid to form a salt with sulfuric acid or dissolves it in high concentration sulfuric acid and pours it into a large amount of water to obtain fine particles using a chemical atomization method and a ball mill, kneader, etc. There is a physical atomization method using mechanical grinding.

〈発明が解決しようとする問題点〉 しかしながら、粗製鋼フタロシアニンを合成し、次いで
顔料化するという方法は、工程上次のような不満足な点
を有する。
<Problems to be Solved by the Invention> However, the method of synthesizing crude steel phthalocyanine and then converting it into a pigment has the following unsatisfactory points in terms of the process.

(1)工程が長く不経済である。(1) The process is long and uneconomical.

(2)顔料化工程で硫酸を使用する場合には、装置の腐
食や大量に発生する廃酸の処理等が公害と関連した重要
な問題として存在する。
(2) When sulfuric acid is used in the pigmentation process, there are important problems related to pollution, such as corrosion of equipment and disposal of waste acid generated in large quantities.

(3)機械的摩砕による顔料化の場合には、処理が煩雑
で、しかも長時間多量の動力を要し、且つ1バッチ当り
の処理量が少なく、非常に生産性が低い。また高COD
廃水の処理等が大きな問題となっている。
(3) In the case of pigment formation by mechanical grinding, the process is complicated, requires a large amount of power over a long period of time, and the throughput per batch is small, resulting in very low productivity. Also high COD
Wastewater treatment has become a major issue.

かかる諸問題を解決する方法として顔料化工程を必要と
しない銅フタロシアニン顔料の直接的製造方法の開発が
期待される。このような背景のもとに種々方法の提案が
なされている(特開昭48−32919号、特公昭50
−1135号、特公昭52−19217号公報)。しか
しながら、これらの提案も、反応役作的にもまた顔料適
性的にも十分満足できる方法ではなかった。
As a method to solve these problems, it is expected to develop a method for directly producing copper phthalocyanine pigments that does not require a pigmentation step. Against this background, various methods have been proposed (Japanese Patent Application Laid-open No. 48-32919,
-1135, Japanese Patent Publication No. 52-19217). However, these proposals were not fully satisfactory in terms of reaction performance and pigment suitability.

〈問題点を解決するための手段〉 本発明者らは、これら従来の銅フタロシアニン顔料の製
造方法における諸欠点を除くために種々検討した結果、
前記した粗製銅フタロシアニンの合成反応系において、
有機溶剤中、特定の物質の共存下に反応させることによ
り、顔料化処理工程を経ることなく、合成で生じた銅フ
タロシアニン粒子を直接顔料として用いるこ々ができる
ことを見出し、本発明を完成したものである。
<Means for Solving the Problems> As a result of various studies by the present inventors in order to eliminate the various drawbacks of these conventional methods for producing copper phthalocyanine pigments, the present inventors have found that:
In the crude copper phthalocyanine synthesis reaction system described above,
The present invention was achieved by discovering that by reacting in the presence of a specific substance in an organic solvent, it is possible to directly use synthesized copper phthalocyanine particles as a pigment without going through a pigmentation process. It is.

すなわち、本発明は、フタル酸及び/又はその誘導体、
尿素、銅またはその化合物を触媒の存在下に有機溶媒中
で反応させて、銅フタロシアニンを製造する際に、下記
一般式で示される化合物を共存させ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, the present invention provides phthalic acid and/or its derivatives,
A method for producing a copper phthalocyanine pigment, which comprises coexisting a compound represented by the following general formula when producing copper phthalocyanine by reacting urea, copper, or a compound thereof in an organic solvent in the presence of a catalyst. be.

〔式中、A及びBは、水素原子、アルキル基、ヒドロキ
シルアルキル基、アルコキシルアルキル基、シクロアル
キル基、アリル基、アラルキル基または−C1l、Y基
(Yはフェニル基又はその誘導体、ナフタレン環又はそ
の誘導体、フタロシアニン環又はそのUs誘導体表わす
。)を表わすが、AとBは同一でも異なっていてもよい
。〕 本発明において使用するフタル酸及び/又はその誘導体
は銅フタロシアニン環を形成し得るもので、例えばフタ
ル酸塩、無水フタル酸、フタルイミド、フタルアミド酸
及びその塩若しくはそのエステル、フタル酸エステル、
フトロニトリル等ヲ挙げることができる。
[In the formula, A and B are a hydrogen atom, an alkyl group, a hydroxylalkyl group, an alkoxylalkyl group, a cycloalkyl group, an allyl group, an aralkyl group or -C1l, a Y group (Y is a phenyl group or a derivative thereof, a naphthalene ring or A and B may be the same or different. ] The phthalic acid and/or its derivatives used in the present invention can form a copper phthalocyanine ring, such as phthalate, phthalic anhydride, phthalimide, phthalamic acid and its salt or its ester, phthalic acid ester,
Examples include phtronitrile and the like.

また、本発明において使用する銅及び/又はその化合物
としては、例えば金属鋼、第−銅又は第二銅のハロゲン
化物、酸化銅、シアン化銅、硫酸銅、硝酸銅、リン酸銅
、酢酸銅、硫化銅、水酸化銅などが挙げられる。また反
応性の乏しい水酸化鋼や酸化銅を使用する時は塩化アン
モニウム等のハロゲン化物を共存させてもよい。銅化合
物等の使用量はフタル酸及び/又はその誘導体4モルあ
たり1〜1.3モル程度である。
Copper and/or its compounds used in the present invention include, for example, metallic steel, cupric or cupric halides, copper oxide, copper cyanide, copper sulfate, copper nitrate, copper phosphate, copper acetate. , copper sulfide, copper hydroxide, etc. Furthermore, when using hydroxide steel or copper oxide, which have poor reactivity, a halide such as ammonium chloride may be allowed to coexist. The amount of the copper compound etc. to be used is about 1 to 1.3 mol per 4 mol of phthalic acid and/or its derivative.

また、本発明に使用される尿素について、その使用量は
フタル酸及び/又はその誘導体4モルあたり4〜40モ
ル程度である。
Further, the amount of urea used in the present invention is about 4 to 40 moles per 4 moles of phthalic acid and/or its derivative.

本発明において使用される触媒としては例えばモリブデ
ン酸アンモニウム、酸化モリブデン、リンモリブデン酸
などのモリブデン化合物、四塩化チタン、チタン酸エス
テル等のチタン化合物、塩化ジルコニウム、炭酸ジルコ
ニウム等のジルコニウム化合物、酸化アンチモン、酸化
ヒ素、ホウ酸などが挙げられる。
Catalysts used in the present invention include, for example, ammonium molybdate, molybdenum oxide, molybdenum compounds such as phosphomolybdic acid, titanium compounds such as titanium tetrachloride and titanate esters, zirconium compounds such as zirconium chloride and zirconium carbonate, antimony oxide, Examples include arsenic oxide and boric acid.

次に本発明に使用される有機溶媒としては、アルキルベ
ンゼン、アルキルナフタレン、テトラリン等の芳香族炭
化水素;アルキルシクロヘキサン、デカリン等の脂環式
炭化水素;デカン、ドデカン等の脂肪族炭化水素;ニト
ロベンゼン、○−ニトロトルエン、トリクロロベンゼン
、ジクロロベンゼン、クロロナフタレン、ジフェニルエ
ーテル、スルホラン、ジメチルスルホキシド、メチルス
ルホラン、ジメチルスルホラン、N−メチルピロリドン
、ジメチルイミダゾリジノン等を挙げることができ、こ
れら2種以上の混合物であってもよい。
Next, the organic solvents used in the present invention include aromatic hydrocarbons such as alkylbenzene, alkylnaphthalene, and tetralin; alicyclic hydrocarbons such as alkylcyclohexane and decalin; aliphatic hydrocarbons such as decane and dodecane; nitrobenzene, -Nitrotoluene, trichlorobenzene, dichlorobenzene, chloronaphthalene, diphenyl ether, sulfolane, dimethylsulfoxide, methylsulfolane, dimethylsulfolane, N-methylpyrrolidone, dimethylimidazolidinone, etc., and mixtures of two or more of these It's okay.

本発明においてフタロシアニン製造時に使用される共存
し得る物質については、前述した一般式(r)で示した
ものが使用できる。
In the present invention, the substances shown in the above-mentioned general formula (r) can be used as the substances that can coexist during the production of phthalocyanine.

これらの具体例としては下記の化合物が例示できる。Specific examples of these include the following compounds.

4、Not、とN02.の混合物 (RSR’  はアルキル基、アリル基、アラルキル基
またはシクロアルキル基等を表わす。〕[Rは水9− 
原子、アルキル基、ヒドロキシルアルキル基、シクロア
ルキル基、アリル基、アラルキル基またはCIL−Y基
等を表わす。
4, Not, and N02. (RSR' represents an alkyl group, an allyl group, an aralkyl group, a cycloalkyl group, etc.)] [R is water 9-
It represents an atom, an alkyl group, a hydroxylalkyl group, a cycloalkyl group, an allyl group, an aralkyl group, a CIL-Y group, or the like.

Yはフェニル基又はその誘導体、ナフタレン環又はその
誘導体、フタロシアニン環又はその誘導体を表わす。〕 ここで、−CI12Yの具体例としてはなどが挙げられ
る。
Y represents a phenyl group or a derivative thereof, a naphthalene ring or a derivative thereof, a phthalocyanine ring or a derivative thereof. ] Here, specific examples of -CI12Y include the following.

(nは1〜18の整数、Rはアルキル基、フェニル基等
を表わす。) これら一般式で示される化合物の使用量は、特に限定さ
れるものではないが、通常フタル酸等に対して、1〜3
0%重量比が好ましい。
(n is an integer of 1 to 18, R represents an alkyl group, a phenyl group, etc.) The amount of the compound represented by these general formulas is not particularly limited, but usually, relative to phthalic acid, etc. 1-3
A weight ratio of 0% is preferred.

本発明の製造方法によれば、通常の粗製銅フタロシアニ
ンを製造する場合と本質的に同じ反応操作により、容易
に目的とする銅フタロシアニン顔料が得られる。
According to the production method of the present invention, the desired copper phthalocyanine pigment can be easily obtained by essentially the same reaction operation as in the production of ordinary crude copper phthalocyanine.

反応温度としては、150〜250℃の範囲で十分であ
る。また前記一般式で示される化合物を加える時期はフ
タロシアニン環が形成される以前であればいつでもよい
As the reaction temperature, a range of 150 to 250°C is sufficient. Further, the compound represented by the above general formula may be added at any time before the phthalocyanine ring is formed.

反応で得られた銅フタロシアニンの取出しについては、
反応マスを減圧下にして溶媒を蒸留除去し、ついで粉体
を温水又は鉱酸水溶液で洗浄、濾過する方法、又は反応
マスを温水等と混合希釈した後、濾過する方法がある。
Regarding the extraction of copper phthalocyanine obtained from the reaction,
There is a method in which the reaction mass is distilled off under reduced pressure to remove the solvent, and then the powder is washed with warm water or an aqueous mineral acid solution and filtered, or a method in which the reaction mass is mixed and diluted with warm water etc. and then filtered.

〈発明の効果〉 本発明の方法により、従来の銅フタロシアニン顔料の製
造方法の場合と比べ、顔料化工程を経ることなく、フタ
ル酸類等を用いた合成反応の工程のみで銅フタロシアニ
ン顔料を得ることができることは、正に驚くべきことで
ある。
<Effects of the Invention> By the method of the present invention, copper phthalocyanine pigments can be obtained only through a synthetic reaction step using phthalic acids, etc., without going through a pigmentation step, compared to the conventional method for producing copper phthalocyanine pigments. It's truly amazing what it can do.

このようにして、得られた銅フタロシアニン顔料を樹脂
、ワニス、プラスチック等目的に応じた媒体中へ分散さ
せることにより、塗料、インキ、プラスチック着色剤等
を製造することができる。
Paints, inks, plastic colorants, etc. can be produced by dispersing the copper phthalocyanine pigment thus obtained into a medium depending on the purpose, such as a resin, varnish, or plastic.

〈実施例〉 以下に実施例、比較例、参考例を挙げる。<Example> Examples, comparative examples, and reference examples are listed below.

なお、例中の部及び%は重量基準、比表面積値はBET
法によるN2気相吸着法を採用した。
In addition, parts and % in the examples are based on weight, and specific surface area values are BET.
The N2 gas phase adsorption method was adopted.

実施例1 無水フタル酸592部、原票740B、塩化第一銅10
5部、モリブデン酸アンモニウム5部、で表される無水
ピロメリット酸ジイミド30部をハイゾールP(日本石
油Gaall)  3,000部へ加え、撹拌下180
℃まで昇温し、同温度で4.0時間加熱した。反応終了
後、減圧下で溶媒を留去し、残渣を2%塩酸5.000
部中に加え、70℃で1時間撹拌したのち吸引濾過した
。ケーキを80℃の温湯で十分洗浄したのち乾燥して銅
フタロシアニン575部を得た。このものの比表面積は
85m’/gであった。
Example 1 592 parts of phthalic anhydride, original form 740B, cuprous chloride 10
5 parts of ammonium molybdate, and 30 parts of pyromellitic anhydride diimide represented by
The temperature was raised to ℃ and heated at the same temperature for 4.0 hours. After the reaction was completed, the solvent was distilled off under reduced pressure, and the residue was dissolved in 2% hydrochloric acid (5.000 g).
After stirring at 70°C for 1 hour, the mixture was filtered under suction. The cake was thoroughly washed with hot water at 80°C and then dried to obtain 575 parts of copper phthalocyanine. The specific surface area of this product was 85 m'/g.

実施例2 実施例1において式 で表されるイミド体40部を用いた以外は、実施例1と
同様にして銅フタロシアニン586部を得た。
Example 2 586 parts of copper phthalocyanine was obtained in the same manner as in Example 1 except that 40 parts of the imide represented by the formula in Example 1 was used.

このものの比表面積を測定したところ80m″/gであ
った。
The specific surface area of this material was measured and found to be 80 m''/g.

実施例3 ハイゾールPに代えて、ニトロベンゼンを溶媒に用いた
以外は実施例1と同様にして、銅フタロシアニン570
部を得た。このものの比表面積は78m’/gであった
Example 3 Copper phthalocyanine 570 was prepared in the same manner as in Example 1 except that nitrobenzene was used as the solvent instead of Hysol P.
I got the department. The specific surface area of this product was 78 m'/g.

実施例4〜9 実施例1において用いたイミド体やノ1イゾールPを他
のイミド体、溶媒に変化させて銅フタロシ〒−・/ a
 ff111 ’A I 、 f−その扶巣を下表にま
とめる。
Examples 4 to 9 Copper phthalocyanate was prepared by changing the imide and Noizole P used in Example 1 to other imides and solvents.
ff111'A I, f-The following table summarizes its support nests.

実施例10 無水フタル酸592部、尿素960部、塩化第一銅10
5部、四塩化チタン50部、下式 で表わされるイミド体30部をスルホラン4.500部
へ加え、撹拌下180〜190℃まで昇温し、同温度で
5時間加熱した。次いで100℃まで冷却し、あらかじ
め60℃に保温した温水5.000部を加える。
Example 10 592 parts of phthalic anhydride, 960 parts of urea, 10 parts of cuprous chloride
5 parts of titanium tetrachloride, and 30 parts of an imide represented by the following formula were added to 4.500 parts of sulfolane, and the temperature was raised to 180 to 190°C with stirring, and heated at the same temperature for 5 hours. Next, cool to 100°C and add 5,000 parts of warm water kept at 60°C in advance.

次いで、反応マスを濾過し、濾過終了後、80℃の温水
5.000部で洗浄する。その後、取出したウェット・
ケーキを2%塩酸5.000部に加え、60℃で1時間
撹拌した後、濾過した。次いで、80℃の温水5.00
0部で洗浄し、乾燥することにより、銅フタロシアニン
575部を得た。得られた化合物の比表面積は90m’
/gであった。
Next, the reaction mass is filtered, and after the filtration is completed, it is washed with 5,000 parts of 80°C warm water. Then, remove the wet
The cake was added to 5.000 parts of 2% hydrochloric acid, stirred at 60°C for 1 hour, and then filtered. Then 80℃ warm water 5.00
By washing with 0 parts and drying, 575 parts of copper phthalocyanine were obtained. The specific surface area of the obtained compound is 90 m'
/g.

実施例11 無水フタル酸592部、尿素960部、塩化第一銅10
5部、四塩化チタン80部及び下記の構造式で表わされ
るイミドメチロール体45部をスルホラン6、000部
へ加え、撹拌下180〜190℃まで昇温し、同温度で
5時間加熱した。次いで100℃まで冷却し、あらかじ
め60℃に保温した温水5.000部を加える。次いで
、反応マスを濾過し、濾過終了。
Example 11 592 parts of phthalic anhydride, 960 parts of urea, 10 parts of cuprous chloride
5 parts of titanium tetrachloride, 80 parts of titanium tetrachloride, and 45 parts of an imidomethylol derivative represented by the following structural formula were added to 6,000 parts of sulfolane, and the temperature was raised to 180 to 190°C with stirring, and heated at the same temperature for 5 hours. Next, cool to 100°C and add 5,000 parts of warm water kept at 60°C in advance. Next, the reaction mass is filtered to complete the filtration.

後、80℃の温水5.000部で洗浄する。その後、取
出したウェット・ケーキを2%塩酸5.000部に加え
、60℃で1時間撹拌した後、濾過した。次いで、80
℃の温水5.000部で洗浄し、乾燥することにより、
銅フタロシアニン590部を得た。得られた化合物の比
表面積は90m’/gであった。
Afterwards, it is washed with 5,000 parts of 80°C warm water. Thereafter, the wet cake taken out was added to 5.000 parts of 2% hydrochloric acid, stirred at 60°C for 1 hour, and then filtered. Then 80
By washing with 5,000 parts of warm water at °C and drying,
590 parts of copper phthalocyanine were obtained. The specific surface area of the obtained compound was 90 m'/g.

実施例12 無水フタル酸592部、尿素960部、塩化第一銅10
5部、四塩化チタン80部、下記の構造式で表わされる
フタロシアニン誘導体60部をスルホラン6、000部
へ加え、撹拌下185℃まで昇温し、同温度で5時間加
熱した。次いで100℃まで冷却し、あらかじめ60℃
に保温した温水5.000部を加える。次いで、反応マ
スを濾過し、濾過終了後、80℃の温水5.000部で
洗浄する。その後、取出したウェット・ケーキを2%塩
酸10.000部に加え、60℃で1時間撹拌した後、
濾過した。次いで、80℃の温水10.000部で洗浄
し、乾燥することにより、銅フタロシアニン600部を
得た。得られた化合物の比表面積は88m’/gであっ
た。
Example 12 592 parts of phthalic anhydride, 960 parts of urea, 10 parts of cuprous chloride
5 parts of titanium tetrachloride, 80 parts of titanium tetrachloride, and 60 parts of a phthalocyanine derivative represented by the following structural formula were added to 6,000 parts of sulfolane, and the temperature was raised to 185° C. with stirring, and heated at the same temperature for 5 hours. Then cool to 100℃ and preheat to 60℃
Add 5,000 parts of warm water to the solution. Next, the reaction mass is filtered, and after the filtration is completed, it is washed with 5,000 parts of 80°C warm water. Thereafter, the removed wet cake was added to 10.000 parts of 2% hydrochloric acid, and after stirring at 60°C for 1 hour,
Filtered. Next, 600 parts of copper phthalocyanine was obtained by washing with 10,000 parts of 80°C warm water and drying. The specific surface area of the obtained compound was 88 m'/g.

実施例13 無水フタル酸592部、尿素800部、塩化第一銅10
0部、モリブデン酸アンモニウム4部および下式で表わ
されるイミド体40部をスルホラン4.500部へ加え
、撹拌下180〜190℃まで昇温し、同温度で5時間
加熱した。次いで100℃まで冷却し、あらかじめ60
℃に保温した温水5.000部を加える。
Example 13 592 parts of phthalic anhydride, 800 parts of urea, 10 parts of cuprous chloride
0 parts, ammonium molybdate, 4 parts, and 40 parts of an imide represented by the following formula were added to 4.500 parts of sulfolane, and the temperature was raised to 180 to 190°C with stirring, and heated at the same temperature for 5 hours. Next, cool to 100℃ and preheat to 60℃.
Add 5,000 parts of warm water kept at ℃.

次いで、反応マスを濾過し、濾過終了後、80℃の温水
5.000部で洗浄する。その後、取出したウェット・
ケーキを2%塩酸8.000部に加え、60℃で1時間
撹拌した後、濾過した。次いで、80℃の温水10.0
00部で洗浄し、乾燥することにより、銅フタロシアニ
ン550部を得た。得られた化合物の比表面積は85m
″/gであった。
Next, the reaction mass is filtered, and after the filtration is completed, it is washed with 5,000 parts of 80°C warm water. Then, remove the wet
The cake was added to 8.000 parts of 2% hydrochloric acid, stirred at 60°C for 1 hour, and then filtered. Then 80℃ warm water 10.0
By washing with 0.00 parts and drying, 550 parts of copper phthalocyanine was obtained. The specific surface area of the obtained compound is 85 m
″/g.

実施例14 無水フタル酸592部、尿素800部、塩化第一銅10
0部、モリブデン酸アンモニウム4部、下式で表わされ
るイミド体30部をジメチルスルホキシド(DMSO)
 6.000部へ加え、撹拌下200〜210℃まで昇
温し、同温度で4時間加熱した。次いで100℃まで冷
却し、あらかじめ60℃に保温した温水10.000s
を加える。次いで、反応マスを濾過し、濾過終了後、8
0℃の温水5.000部で洗浄する。その後、取出した
ウェット・ケーキを1%塩酸10.000部に加え、6
0℃で1時間撹拌した後、濾過した。次いで、80℃の
温水10.000部で洗浄し、乾燥することにより、銅
フタロシアニン530部を得た。得られた化合物の比表
面積は、85m’/gであった。
Example 14 592 parts of phthalic anhydride, 800 parts of urea, 10 parts of cuprous chloride
0 parts, ammonium molybdate 4 parts, and 30 parts of the imide represented by the following formula in dimethyl sulfoxide (DMSO)
The mixture was added to 6.000 parts, heated to 200 to 210°C with stirring, and heated at the same temperature for 4 hours. Then cooled to 100℃ and heated water previously kept at 60℃ for 10,000 seconds.
Add. Next, the reaction mass was filtered, and after the filtration was completed, 8
Wash with 5,000 parts of warm water at 0°C. Then, add the removed wet cake to 10.000 parts of 1% hydrochloric acid and
After stirring at 0°C for 1 hour, it was filtered. Next, 530 parts of copper phthalocyanine was obtained by washing with 10,000 parts of 80°C warm water and drying. The specific surface area of the obtained compound was 85 m'/g.

実施例15 無水フタル酸592部、尿素800部、臭化第一銅14
0部、四塩化チタン10部、下式で表わされるイミド体
30部をスルホラン5.500部へ加え、撹拌下180
〜190℃まで昇温し、同温度で5時間加熱した。次い
で100℃まで冷却し、あらかじめ60℃に保温した温
水5.000部を加える。次いで、反応マスを濾過し、
濾過終了後、80℃の温水10.000部で洗浄する。
Example 15 592 parts of phthalic anhydride, 800 parts of urea, 14 parts of cuprous bromide
0 parts, titanium tetrachloride 10 parts, and 30 parts of an imide compound represented by the following formula were added to 5.500 parts of sulfolane, and 180 parts of titanium tetrachloride was added under stirring.
The temperature was raised to ~190°C and heated at the same temperature for 5 hours. Next, cool to 100°C and add 5,000 parts of warm water kept at 60°C in advance. The reaction mass is then filtered,
After filtration, wash with 10,000 parts of 80°C warm water.

その後、取出したウェット・ケーキを2%塩酸10.0
00部に加え、60℃で1時間撹拌した後、濾過した。
After that, the removed wet cake was mixed with 2% hydrochloric acid 10.0
00 parts, stirred at 60°C for 1 hour, and then filtered.

次いで、80℃の温水10.000部で洗浄し、乾燥す
ることにより、銅フタロシアニン580部を得た。得ら
れた化合物の比表面積は85m’/gであった。
Next, 580 parts of copper phthalocyanine was obtained by washing with 10,000 parts of 80°C warm water and drying. The specific surface area of the obtained compound was 85 m'/g.

参考例−1 実施例−1において、使用した無水ピロメリット酸ジイ
ミドを存在させずに反応を行ない銅フタロシアニン57
0部を得た。このものの比表面積を測定したところ24
m’/gであった。
Reference Example-1 In Example-1, the reaction was carried out in the absence of the pyromellitic anhydride diimide used, and copper phthalocyanine 57
I got 0 copies. When the specific surface area of this material was measured, it was 24
m'/g.

参考例−2 実施例−10において、使用した無水ピロメリット酸ジ
イミドを存在させずに反応を行ない銅フタロシアエフ5
60部を得た。このものの比表面積を測定したところ2
5m’/gであった。
Reference Example-2 In Example-10, the reaction was carried out in the absence of the pyromellitic anhydride diimide used, and copper phthalocyanaf 5
Got 60 copies. When the specific surface area of this material was measured, it was found that 2
It was 5 m'/g.

比較例−1 市販の粗製銅フタロシアニン100部、食塩400部、
エチレングリコール100部を実験用双腕型ニーグーで
80〜85℃を維持しながら、5時間摩砕した。混合物
を80℃の温水で洗浄した後乾燥して銅フタロシアニン
顔料98部を得た。比表面積70m’/gであった。
Comparative Example-1 100 parts of commercially available crude copper phthalocyanine, 400 parts of common salt,
100 parts of ethylene glycol was ground for 5 hours while maintaining a temperature of 80 to 85°C in a double-armed experimental Ni-Goo. The mixture was washed with warm water at 80°C and dried to obtain 98 parts of copper phthalocyanine pigment. The specific surface area was 70 m'/g.

かくして得られた銅フタロシアニン顔料4部、チタン白
80部及び亜麻仁油160部よりインキを調製した。こ
の着色力を測定し、これを100として、実施例や参考
例で得られた銅フタロシアニンも同様にインキ化して着
色力を測定した。
An ink was prepared from 4 parts of the copper phthalocyanine pigment thus obtained, 80 parts of titanium white, and 160 parts of linseed oil. This coloring power was measured, and using this value as 100, the copper phthalocyanine obtained in Examples and Reference Examples was also formed into ink and the coloring power was measured.

比較例−2 比較例−1で得た銅フタロシアニン顔料4部を直(?4
3 mmのガラスピーズ90部の入ったポリ瓶に入れ、
メラミンアルキッド系塗料フェス12部とキシレン14
ffr!、を加えて、ペイントシェーカーにかけ1時間
運転して後、同じメラミンアルキッドワニス50部を加
えてさらに10分運転した。その後金網でガラスピーズ
をこし別け、青の原色塗料を得た。
Comparative Example-2 4 parts of the copper phthalocyanine pigment obtained in Comparative Example-1 was directly added (?4 parts).
Place it in a plastic bottle containing 90 parts of 3 mm glass beads.
Melamine alkyd paint festival 12 parts and xylene 14 parts
ffr! , and the paint shaker was run for 1 hour, then 50 parts of the same melamine alkyd varnish was added and the run was run for an additional 10 minutes. He then strained the glass peas through a wire mesh to obtain blue primary color paint.

この原色塗料3部とチタン白30%を含む同系の白塗料
5部をガラス棒でよく混合して青色塗料を作った。
Three parts of this primary color paint and five parts of a white paint of the same type containing 30% titanium white were thoroughly mixed with a glass rod to make a blue paint.

次に、実施例−10、参考例−1で得た銅フタロシアニ
ンも同様にして塗料を作った。
Next, paints were made using the copper phthalocyanine obtained in Example 10 and Reference Example 1 in the same manner.

これらの着色力比較を行った結果、次の通りであった。The results of comparing these coloring powers were as follows.

比較例−2100% 実施例−10110% 参考例−130% I  lComparative example - 2100% Example-10110% Reference example - 130% I l

Claims (1)

【特許請求の範囲】 フタル酸及び/又はその誘導体、尿素、銅又はその化合
物を触媒の存在下に有機溶媒中で反応させて銅フタロシ
アニンを製造する際に、下記一般式で示される化合物の
共存下に反応させることを特徴とする銅フタロシアニン
顔料の製造方法。 一般式 ▲数式、化学式、表等があります▼ 〔式中、A及びBは、水素原子、アルキル基、ヒドロキ
シルアルキル基、アルコキシルアルキル基、シクロアル
キル基、アリル基、アラルキル基または−CH_2Y基
(Yはフェニル基又はその誘導体、ナフタレン環又はそ
の誘導体、フタロシアニン環又はその誘導体を表わす)
を表わすが、AとBとは同一でも異なっていてもよい。 〕
[Claims] When producing copper phthalocyanine by reacting phthalic acid and/or its derivatives, urea, copper, or its compounds in an organic solvent in the presence of a catalyst, the coexistence of a compound represented by the following general formula A method for producing a copper phthalocyanine pigment, characterized by carrying out the following reaction. General formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [In the formula, A and B are hydrogen atoms, alkyl groups, hydroxylalkyl groups, alkoxylalkyl groups, cycloalkyl groups, allyl groups, aralkyl groups, or represents a phenyl group or its derivatives, a naphthalene ring or its derivatives, a phthalocyanine ring or its derivatives)
, but A and B may be the same or different. ]
JP4222187A 1986-10-31 1987-02-24 Production of copper phthalocyanine pigment Pending JPS63207858A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP4222187A JPS63207858A (en) 1987-02-24 1987-02-24 Production of copper phthalocyanine pigment
US07/110,528 US4785091A (en) 1986-10-31 1987-10-20 Process for producing copper phthalocyanine pigment
DE8787309637T DE3787072D1 (en) 1986-10-31 1987-10-30 METHOD FOR PRODUCING A COPPER PHTHALOCYANINE PIGMENT.
EP87309637A EP0266219B1 (en) 1986-10-31 1987-10-30 Process for producing copper phthalocyanine pigment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4222187A JPS63207858A (en) 1987-02-24 1987-02-24 Production of copper phthalocyanine pigment

Publications (1)

Publication Number Publication Date
JPS63207858A true JPS63207858A (en) 1988-08-29

Family

ID=12629983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4222187A Pending JPS63207858A (en) 1986-10-31 1987-02-24 Production of copper phthalocyanine pigment

Country Status (1)

Country Link
JP (1) JPS63207858A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01254773A (en) * 1988-04-05 1989-10-11 Dainichiseika Color & Chem Mfg Co Ltd Production of low chlorinated copper phthalocyanine blue pigment
US5318623A (en) * 1992-05-29 1994-06-07 Toyo Ink Manufacturing Co., Ltd. Process for producing metal phthalocyanine pigment
EP0783029A1 (en) * 1996-01-08 1997-07-09 Dainippon Ink And Chemicals, Inc. Production method of beta-type copper phthalocyanine pigment
JP2000007677A (en) * 1998-06-02 2000-01-11 Ciba Specialty Chem Holding Inc Direct production of pyrrolo[3,4-c]pyrrole
US8168359B2 (en) 2008-03-10 2012-05-01 Xerox Corporation Nanosized particles of phthalocyanine pigments
US8809523B2 (en) 2008-03-10 2014-08-19 Xerox Corporation Method of making nanosized particles of phthalocyanine pigments

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01254773A (en) * 1988-04-05 1989-10-11 Dainichiseika Color & Chem Mfg Co Ltd Production of low chlorinated copper phthalocyanine blue pigment
US5318623A (en) * 1992-05-29 1994-06-07 Toyo Ink Manufacturing Co., Ltd. Process for producing metal phthalocyanine pigment
EP0783029A1 (en) * 1996-01-08 1997-07-09 Dainippon Ink And Chemicals, Inc. Production method of beta-type copper phthalocyanine pigment
US5831083A (en) * 1996-01-08 1998-11-03 Dainippon Ink And Chemicals, Inc. Production method of beta-type copper phthalocyanine pigment
JP2000007677A (en) * 1998-06-02 2000-01-11 Ciba Specialty Chem Holding Inc Direct production of pyrrolo[3,4-c]pyrrole
JP2011038096A (en) * 1998-06-02 2011-02-24 Ciba Holding Inc DIRECT MANUFACTURE OF PYRROLO[3,4-c]PYRROLE
US8168359B2 (en) 2008-03-10 2012-05-01 Xerox Corporation Nanosized particles of phthalocyanine pigments
US8809523B2 (en) 2008-03-10 2014-08-19 Xerox Corporation Method of making nanosized particles of phthalocyanine pigments

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