JPS647108B2 - - Google Patents
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- Publication number
- JPS647108B2 JPS647108B2 JP3527881A JP3527881A JPS647108B2 JP S647108 B2 JPS647108 B2 JP S647108B2 JP 3527881 A JP3527881 A JP 3527881A JP 3527881 A JP3527881 A JP 3527881A JP S647108 B2 JPS647108 B2 JP S647108B2
- Authority
- JP
- Japan
- Prior art keywords
- copper phthalocyanine
- parts
- type
- phthalocyanine
- point
- 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
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- Nitrogen Condensed Heterocyclic Rings (AREA)
Description
本発明はε型のX線回折スペクトルを有する銅
フタロシアニンを純粋に、しかも低廉かつ安全、
無公害なプロセスで工業的規模で製造する方法に
関する。
純粋なε型銅フタロシアニンは、α型銅フタロ
シアニンより更に赤味の色調を有し、鮮明で着色
力も高い上に結晶転位に対してもより安定なの
で、極めて好ましい性質を持つた銅フタロシアニ
ンであると評価されている。
ε型銅フタロシアニンを製造する方法はこれま
でにも種々提案されているが、純粋なε型を得る
工業的製造法という観点からみると、いずれも極
めて不満足なものであつた。
例えば、α型或いはγ型等の、一旦顔料化工程
を経た銅フタロシアニンを原料として、ε型への
結晶転位を行わせる英国特許第1411880号、日本
特公昭52―6300、特公昭52―6301に記載されてい
る方法は、たとえ純粋なε型銅フタロシアニンが
得られるにせよ、極めてコスト高になることはさ
けられないし、β型の粗製銅フタロシアニンをε
型に結晶転位せしめるドイツ特許第1181248号記
載の方法では、純粋なε型銅フタロシアニンを得
ることは不可能である。
無水フタル酸或いはフタロジニトリルを出発原
料として、最初からε型銅フタロシアニンを目的
として合成する方法は有利な方法であかに考えら
れるが、フタロジニトリルと尿素、銅塩を熔融状
態でコニーダー等に通し高剪断力の下に反応せし
める米国特許第3051721号記載の方法は、反応が
極めて短時間に終り、しかもその間の一時期にし
か高剪断力がかかり得る粘度状態が存在しないの
で、制御が極めて難かしく実用的でない。また熔
融尿素を溶媒として無水フタル酸或いはフタロジ
ニトリル等の原料を少量づつ添加して反応せしめ
る特公昭40―2780記載の方法は、安定してε型結
晶が出来ない上に極めて生産効率が悪くこれ又実
用的でない。
唯一つ、ニトロベンゼンを溶媒に無水フタル
酸、尿素、銅塩及び反応触媒を、銅フタロシアニ
ンスルホクロリドとアミンとの縮合反応物の存在
下に加熱撹拌して、ε型銅フタロシアニンを一段
で合成する特開昭53―39325記載の方法は、工業
的価値を持つ方法と思われるが、この方法の欠点
は、ニトロベンゼン以外の溶媒では純粋なε型銅
フタロシアニンが得られないことである。即ち、
反応に使用する溶媒の種類と結晶系改質剤である
銅フタロシアニンスルホクロリドとアミンとの縮
合反応物の製造に用いられるアミンの種類との組
合せは、得られるε型銅フタロシアニンの純粋度
と反応収率に、極めて大きな影響を持ち、純粋な
ε型銅フタロシアニンを高収率で与える組合せ
は、前記特開昭53―39325の方法ではニトロベン
ゼン溶媒とデヒドロアビエチルアミンとの組合せ
しかなく、ニトロベンゼンを用いたとしても他の
組合せでは収率が著るしく低いか、或いはβ型と
の混合でしか得られない。ところがニトロベンゼ
ンは毒性が大きく、これを溶媒として工業的に用
いることは労働安全衛生上の問題が大きく、ま
た、工場排水の処理に多大の費用を要するため実
用的でない。しかも、使用された結晶系改質剤は
最終製品迄そのまま混入して来るので、銅フタロ
シアニンスルホクロリドとデヒドロアビエチルア
ミンとの縮合物の如く、極めて油溶性の高い化合
物は、顔料の耐ブリード性を損うことになり好ま
しくない。
本発明者らは労働安全衛生上の見地から毒性が
低く、且つニトロベンゼン或いは塩素系溶媒の如
き公害問題を与えないアルキルベンゼンを溶媒と
して用い、耐ブリード性に実用上問題がなく、且
つ純粋にε型のX線回折スペクトルを示す銅フタ
ロシアニンを、安定に、高収率で得られる方法を
鋭意検討した結果、通常の無水フタル酸―尿素―
アルキルベンゼン溶媒法に於て、結晶系改質剤と
して油溶性の低い銅フタロシアニンスルホクロリ
ドと芳香族アミンとの縮合反応物を用い、予め製
造されたBET法による比表面積が35m2/g以下
のε型銅フタロシアニン粗製顔料をシード結晶と
して一定量、最初から添加することにより目的を
達成することができた。
本発明方法において用いられる結晶系改質剤
は、下記一般式()で表される化合物であり、
(式中、Pcは金属又は金属不含フタロシアニ
ン残基を表わし、Mは水素原子又はアルカル金属
原子或いはアンモニウム基を表わし、R1,R2は
水素原子、ハロゲン原子、アルキル基、アルコキ
シ基、アルカノール基を表わし、x及びyは0な
いし4、zは1ないし4の数字を表わすが、x,
y,zの合計は1ないし4の範囲にある。)
特にPcが銅フタロシアニンであるものが好ま
しい。
この化合物は、粗製銅フタロシアニンをクロル
スルホン酸と塩化チオニルで処理し、生成した銅
フタロシアニンスルホクロリドを芳香族アミンと
反応させる通常の方法で製造することができる。
用いられる芳香族アミンとしては、アニリン、
o,p―トルイジン、o,m,p―クロルアニリ
ン、o,m,p―ブロムアニリン、o,p―アニ
シジン、2,4―ジクロルアニリン、3,5―ジ
クロルアニリン、2,4―ジブロムアニリン、
3,5―ジブロムアニリン、2,4―キシリジン
等があげられるが、アニリンが特に有用である。
置換基の数は、x,yがそれぞれ0ないし4、
zが1ないし4で且つx,y,zの合計が1ない
し4であるが、特にx,yが0に近く、zが1な
いし2のものが好ましい。
シード結晶としてのε型銅フタロシアニン粗製
顔料は、BET法による比表面積が35m2/g以下
の純粋なε型銅フタロシアニンであればよく、生
成した顔料を乾燥、粉砕して粉末状としたもので
も、生成した顔料を含む反応終了液のまゝでも使
用できる。
溶媒のアルキルベンゼンは、本発明の製造方法
における反応条件である150〜200℃、3〜8時
間、該反応系中で不活性であることが必要なこと
から、沸点150〜250℃のものを用いる。具体例と
しては、イソプロピルキシレン、ジイソプロピル
トルエン、t―アルミベンゼン、t―ヘキシルベ
ンゼン、2―エチルヘキシルベンゼン等があげら
れるほか、ソルベツソ150等の如く沸点範囲を持
つ混合物であつても良い。使用量はフタロシアニ
ン環形成性の有機化合物に対し重量で2ないし5
倍量が適当である。
本発明方法において用いられるフタロシアニン
環を形成し得る有機化合物は、従来から知られて
いるフタル酸、無水フタル酸、フタルイミド、フ
タル酸ジアミド、フタラミド酸、o―シアノ安息
香酸、フタロジニトリルなどであるが、特に無水
フタル酸が好ましい。
銅化合物は、無水塩化第一銅、無水塩化第二
銅、酸化銅、亜酸化銅、水酸化銅、硫酸化銅等、
従来から銅フタロシアニンの銅原子供給化合物と
して知られているものが、フタロシアニン環形成
性の有機化合物4モルに対し0.9ないし1.05モル
程度の範囲で使用される。
反応触媒についても、従来から知られているも
のがいずれも使用可能であるが、モリブデン酸ア
ンモン又は酸化モリブデンが有用であり、使用量
はフタロシアニン環形成性有機化合物4モルに対
し、0.01ないし0.03モルが適当である。
結晶改質剤とε型銅フタロシアニンシード結晶
の使用量は、両者のバランスに基く特定の範囲内
とすることが特に重要であり、その範囲は以下の
如く特定される。
即ち、フタロシアニン環形成性有機化合物に対
し重量比で、結晶系改質剤の使用割合を横軸
(X)にとり、ε型銅フタロシアニンシード結晶
使用割合を縦軸(Y)にとつた場合、点A(X=
4.0%、Y=6.0%)と点B(X=4.0%、Y=10%)
とを結ぶ直線と点A(X=4.0%、Y=6.0%)と
点C(X=10%、Y=6.0%)とを結ぶ直線にはさ
まれた範囲(但し、X≧4.0%、Y≧6.0%)が使
用可能範囲で、この範囲内であれば自由に両化合
物の割合を選定することが出来る。しかし必要以
上に使用することは無駄であるばかりでなく、特
に結晶系改質剤の過剰は、最終製品の耐ブリード
性に良い影響を与えないので、これらの使用量は
必要最低限に押えることが望ましく、通常、標準
的な品質の場合は結晶系改質剤、ε型銅フタロシ
アニンシード結晶共に6%、或いは前者5%、後
者6%の割合で使用される。結晶系改質剤の種類
や反応条件、反応設備等の因子により適宜増減さ
れうることは云うまでもない。両化合物を前記特
定範囲外で使用した場合には、β型又はπ型、或
いはこれらとε型の混合結晶を得ることが多く、
目的とする純粋なε型結晶も持つ銅フタロシアニ
ンを安定して得ることができない。
合成反応は、効率の優れた大型の撹拌機を持つ
反応釜を使用し、冷時原料を加えて、撹拌下に加
熱し、150℃ないし200℃として、3時間ないし8
時間保つ極く普通の方法で行われる。結晶系改質
剤とε型シード結晶の添加は、130℃以下の時点
なら何時でも良く、最初から加えておくのが便利
である。
本発明方法により得られたε型銅フタロシアニ
ンはBET法による比表面積が通常35m2/g以下
であり、そのままでも顔料として使用出来るが、
米国特許第2556730号、同第2982666号等に記載さ
れた公知の方法で、一次結晶をより小さくする磨
砕処理を行なつてから使用するとより鮮明、より
高濃度に着色することが出来る。
本発明方法により得られたε型銅フタロシアニ
ンは、合成又は天然の高分子物質又はその他の有
機化合物、或いは無機物の着色に有用である他、
印刷インキ、塗料用の着色剤としても極めて有用
である。
次に実施例により本発明を説明する。各実施例
において%及び部はいずれも重量%及び重量部を
表わす。
実施例 1
ガラス製オートクレーブに、90℃に保つたステ
ンレス鋼製の保温還流冷却器を付し、無水フタル
酸120部、尿素156部、無水塩化第一銅20.3部モリ
ブデン酸アンモン0.8部及び、ターシヤリーヘキ
シルベンゼン300部を加えて撹拌し、BET法によ
る比表面積24.5m2/gのε型銅フタロシアニン粗
製顔料粉末7.4部と式()で表わされる
化合物6.0部を加えて、30分で110℃に昇温し、
同温度に30分保つて後、1時間で165℃に昇温、
同温度で4時間撹拌した。反応中還流冷却器先端
に取り付けられた調圧弁を操作して、内圧が3.0
Kg/cm2を越えない様にした。冷却後過し、メタ
ノールで充分洗つてから、3000部の水に撹拌分散
し、35%塩酸170部を加えて、90℃で2時間撹拌
して後過し、充分水洗して80℃で乾燥した。
純粋なε型X線回折スペクトルを示す美麗な銅
フタロシアニン114部を得た。この顔料のBET法
による比表面積は20.3m2/gであつた。
実施例 2
実施例1で使用したのと同じ反応装置に、フタ
ルイミド120部、尿素104部、塩化第二銅27.2部、
モリブデン酸アンモン0.8部、ジイソプロピルト
ルエン300部を加えて撹拌した。次いで実施例1
と同様の操作により、反応が終了した時点の生成
ε型銅フタロシアニンを含む液を、ε型銅フタロ
シアニンの含有量が12部となるような量添加し、
更に式()で表わされる化合物12部、
を加え、後実施例1と同様に操作して、純粋なε
型のX線回折スペクトルを示す銅フタロシアニン
122部を得た。この顔料のBET法による比表面積
は28.6m2/gであつた。
実施例 3
実施例1で使用したのと同じ反応装置に無水フ
タル酸120部、尿素156部、無水硫酸銅32.2部、モ
リブデン酸アンモン0.8部、2―エチルヘキシル
ベンゼン300部を加えて撹拌し、実施例2で得た
ε型銅フタロシアニン粗顔料粉末7.2部、式()
で表わされる化合物7.2部を加えた。30分で110℃
まで昇温し、同温度で30分撹拌して後1時間で
180℃に昇温し、同温度で更に4時間撹拌した。
反応中に発生したガスは、還流冷却器先端の調圧
弁を開いて、系外に放出した。実施例1と同様に
処理して純粋なε型のX線回折スペクトルを示す
銅フタロシアニン109部を得た。この顔料のBET
法による比表面積は18.5m2/gであつた。
実施例 4
実施例1で使用したのと同じ反応装置にフタル
イミド120部、尿素104部、水酸化銅19.7部、モリ
ブデン酸アンモン0.8部、ソルベツソ150,300部
を加えて撹拌し、実施例3と同様にして得た、ε
型銅フタロシアニン12部を含む合成反応終了液と
式()
で表わされる化合物9.6部を加えた。実施例3と
同様に操作して、純粋なε型X線回折スペクトル
を示す銅フタロシアニン108部を得た。この顔料
のBET法による比表面積は17.8m2/gであつた。
実施例 5〜10
結晶系改質剤とε型銅フタロシアニン粗製顔料
粉末の量をかえて、実施例1の操作を繰り返し
た。
The present invention produces copper phthalocyanine having an ε-type X-ray diffraction spectrum in a pure, inexpensive and safe manner.
Concerning a method for manufacturing on an industrial scale in a non-polluting process. Pure ε-type copper phthalocyanine has a more reddish color tone than α-type copper phthalocyanine, is clear and has high coloring power, and is more stable against crystal dislocation, so it is considered to be a copper phthalocyanine with extremely desirable properties. It is evaluated. Although various methods for producing ε-type copper phthalocyanine have been proposed, all of them have been extremely unsatisfactory from the viewpoint of industrial production methods for obtaining pure ε-type copper phthalocyanine. For example, British Patent No. 1411880, Japanese Patent Publication No. 52-6300, Japanese Patent Publication No. 52-6301, which uses α-type or γ-type copper phthalocyanine that has undergone a pigmentation process as a raw material to undergo crystal rearrangement to ε-type. Even though the described method yields pure ε-type copper phthalocyanine, it is unavoidable that the cost is extremely high, and the crude β-type copper phthalocyanine can be converted into ε-type copper phthalocyanine.
It is not possible to obtain pure ε-type copper phthalocyanine using the method described in German Patent No. 1,181,248, which causes crystal rearrangement in the form. The method of synthesizing ε-type copper phthalocyanine from the beginning using phthalic anhydride or phthalodinitrile as a starting material is considered to be an advantageous method, but it is possible to synthesize phthalodinitrile, urea, and copper salt in a molten state using a co-kneader, etc. The method described in US Pat. No. 3,051,721, in which the reaction is carried out under high shear force, is extremely difficult to control because the reaction is completed in an extremely short period of time, and there is only a viscosity state during which high shear force can be applied. It's strange and impractical. Furthermore, the method described in Japanese Patent Publication No. 40-2780, in which raw materials such as phthalic anhydride or phthalodinitrile are added little by little using molten urea as a solvent, does not produce stable ε-type crystals and is extremely inefficient. This is also not practical. The only special method is to synthesize ε-type copper phthalocyanine in one step by heating and stirring phthalic anhydride, urea, copper salt, and a reaction catalyst in nitrobenzene as a solvent in the presence of a condensation reaction product of copper phthalocyanine sulfochloride and an amine. Although the method described in 1973-39325 is considered to be of industrial value, the drawback of this method is that pure ε-type copper phthalocyanine cannot be obtained using solvents other than nitrobenzene. That is,
The combination of the type of solvent used in the reaction and the type of amine used in the production of the condensation reaction product of copper phthalocyanine sulfochloride, which is a crystal system modifier, and an amine will affect the purity of the resulting ε-type copper phthalocyanine and the reaction. The combination that has an extremely large effect on the yield and provides a high yield of pure ε-type copper phthalocyanine is the combination of nitrobenzene solvent and dehydroabiethylamine in the method of JP-A-53-39325 mentioned above, and the combination that uses nitrobenzene Even if it is, the yield is extremely low with other combinations, or it can only be obtained by mixing with the β type. However, nitrobenzene is highly toxic, and its industrial use as a solvent poses serious problems in terms of occupational safety and health, and it is not practical because treatment of industrial wastewater requires a large amount of cost. Moreover, since the crystalline modifier used is directly mixed into the final product, highly oil-soluble compounds such as the condensate of copper phthalocyanine sulfochloride and dehydroabiethylamine may affect the bleed resistance of the pigment. This is not desirable as it will cause a loss. The present inventors used an alkylbenzene as a solvent, which has low toxicity from the standpoint of occupational safety and health and does not cause pollution problems like nitrobenzene or chlorinated solvents, and has no practical problems with bleed resistance, and is a pure ε-type solvent. As a result of intensive research on a method to obtain copper phthalocyanine stably and in high yield, which exhibits an X-ray diffraction spectrum of
In the alkylbenzene solvent method, a condensation reaction product of copper phthalocyanine sulfochloride, which has low oil solubility, and an aromatic amine is used as a crystal system modifier, and a pre-produced ε having a specific surface area of 35 m 2 /g or less by the BET method is used. The objective was achieved by adding a certain amount of copper phthalocyanine crude pigment as seed crystals from the beginning. The crystalline modifier used in the method of the present invention is a compound represented by the following general formula (), (In the formula, Pc represents a metal or metal-free phthalocyanine residue, M represents a hydrogen atom, an alkali metal atom, or an ammonium group, and R 1 and R 2 represent a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group, an alkanol represents a group, x and y represent a number from 0 to 4, z represents a number from 1 to 4, but x,
The sum of y and z is in the range of 1 to 4. ) Particularly preferred is one in which Pc is copper phthalocyanine. This compound can be produced by a conventional method in which crude copper phthalocyanine is treated with chlorosulfonic acid and thionyl chloride, and the resulting copper phthalocyanine sulfochloride is reacted with an aromatic amine. Aromatic amines used include aniline,
o,p-toluidine, o,m,p-chloroaniline, o,m,p-bromoaniline, o,p-anisidine, 2,4-dichloroaniline, 3,5-dichloroaniline, 2,4- dibromoaniline,
Examples include 3,5-dibromoaniline and 2,4-xylidine, with aniline being particularly useful. The number of substituents is 0 to 4 for x and y, respectively;
Although z is 1 to 4 and the sum of x, y, and z is 1 to 4, it is particularly preferable that x, y are close to 0 and z is 1 to 2. The crude ε-type copper phthalocyanine pigment used as a seed crystal may be pure ε-type copper phthalocyanine with a specific surface area of 35 m 2 /g or less by the BET method, or it may be obtained by drying and pulverizing the produced pigment into powder. The reaction solution containing the produced pigment can also be used as it is. The alkylbenzene used as a solvent needs to be inactive in the reaction system under the reaction conditions of 150 to 200°C for 3 to 8 hours in the production method of the present invention, so an alkylbenzene with a boiling point of 150 to 250°C is used. . Specific examples include isopropylxylene, diisopropyltoluene, t-aluminumbenzene, t-hexylbenzene, 2-ethylhexylbenzene, and mixtures having a boiling point range such as Solbetsuso 150 may also be used. The amount used is 2 to 5 by weight based on the phthalocyanine ring-forming organic compound.
Double the amount is appropriate. The organic compounds capable of forming a phthalocyanine ring used in the method of the present invention include conventionally known phthalic acid, phthalic anhydride, phthalimide, phthalic diamide, phthalamic acid, o-cyanobenzoic acid, phthalodinitrile, etc. However, phthalic anhydride is particularly preferred. Copper compounds include anhydrous cuprous chloride, anhydrous cupric chloride, copper oxide, cuprous oxide, copper hydroxide, copper sulfate, etc.
A compound conventionally known as a copper atom supplying compound for copper phthalocyanine is used in an amount of about 0.9 to 1.05 moles per 4 moles of the phthalocyanine ring-forming organic compound. As for the reaction catalyst, any conventionally known catalyst can be used, but ammonium molybdate or molybdenum oxide is useful, and the amount used is 0.01 to 0.03 mol per 4 mol of the phthalocyanine ring-forming organic compound. is appropriate. It is particularly important that the amounts of the crystal modifier and the ε-type copper phthalocyanine seed crystals be within a specific range based on the balance between the two, and this range is specified as follows. In other words, when the horizontal axis (X) is the proportion of the crystalline modifier used in relation to the phthalocyanine ring-forming organic compound and the vertical axis (Y) is the proportion of the ε-type copper phthalocyanine seed crystal used, the point is A(X=
4.0%, Y=6.0%) and point B (X=4.0%, Y=10%)
The range sandwiched between the straight line connecting point A (X=4.0%, Y=6.0%) and point C (X=10%, Y=6.0%) (however, X≧4.0%, Y≧6.0%) is the usable range, and the ratio of both compounds can be freely selected within this range. However, using more than necessary is not only wasteful, but especially an excess of crystalline modifiers will not have a positive effect on the bleed resistance of the final product, so the amount used should be kept to the minimum necessary. Usually, in the case of standard quality, both the crystalline modifier and the ε-type copper phthalocyanine seed crystal are used at a ratio of 6%, or 5% of the former and 6% of the latter. Needless to say, the amount can be increased or decreased as appropriate depending on factors such as the type of crystalline modifier, reaction conditions, and reaction equipment. When both compounds are used outside the specified range, β-type or π-type, or mixed crystals of these and ε-type are often obtained.
It is not possible to stably obtain the desired copper phthalocyanine that also has pure ε-type crystals. For the synthesis reaction, a reaction vessel equipped with a large and highly efficient stirrer is used, and the cold raw materials are added and heated to 150°C to 200°C for 3 to 8 hours.
It is done in a very ordinary way to keep time. The crystal system modifier and the ε-type seed crystal can be added at any time when the temperature is below 130°C, and it is convenient to add them from the beginning. The ε-type copper phthalocyanine obtained by the method of the present invention usually has a specific surface area of 35 m 2 /g or less by the BET method, and can be used as a pigment as it is.
By performing a grinding treatment to make the primary crystals smaller by a known method described in US Pat. No. 2,556,730, US Pat. The ε-type copper phthalocyanine obtained by the method of the present invention is useful for coloring synthetic or natural polymeric substances, other organic compounds, or inorganic substances.
It is also extremely useful as a coloring agent for printing inks and paints. Next, the present invention will be explained with reference to Examples. In each example, both % and parts represent weight % and parts by weight. Example 1 A glass autoclave was equipped with a stainless steel thermal reflux condenser kept at 90°C, and 120 parts of phthalic anhydride, 156 parts of urea, 20.3 parts of anhydrous cuprous chloride, 0.8 parts of ammonium molybdate, and Tarsia were added. Add 300 parts of lyhexylbenzene and stir to obtain 7.4 parts of ε-type copper phthalocyanine crude pigment powder with a specific surface area of 24.5 m 2 /g by the BET method and expressed by the formula (). Add 6.0 parts of the compound and raise the temperature to 110°C for 30 minutes.
After keeping at the same temperature for 30 minutes, the temperature was raised to 165℃ in 1 hour.
The mixture was stirred at the same temperature for 4 hours. During the reaction, operate the pressure regulating valve attached to the tip of the reflux condenser to reduce the internal pressure to 3.0.
I made sure not to exceed Kg/cm 2 . After cooling, filter, thoroughly wash with methanol, stir and disperse in 3,000 parts of water, add 170 parts of 35% hydrochloric acid, stir at 90°C for 2 hours, filter, thoroughly wash with water, and dry at 80°C. did. 114 parts of beautiful copper phthalocyanine showing a pure ε-type X-ray diffraction spectrum was obtained. The specific surface area of this pigment determined by the BET method was 20.3 m 2 /g. Example 2 Into the same reactor used in Example 1, 120 parts of phthalimide, 104 parts of urea, 27.2 parts of cupric chloride,
0.8 parts of ammonium molybdate and 300 parts of diisopropyltoluene were added and stirred. Next, Example 1
By the same operation as above, add the solution containing the ε-type copper phthalocyanine produced at the time the reaction is completed in an amount such that the content of ε-type copper phthalocyanine is 12 parts,
Furthermore, 12 parts of a compound represented by formula (), was added and then operated in the same manner as in Example 1 to obtain pure ε
Copper phthalocyanine showing X-ray diffraction spectrum of type
Obtained 122 copies. The specific surface area of this pigment determined by the BET method was 28.6 m 2 /g. Example 3 120 parts of phthalic anhydride, 156 parts of urea, 32.2 parts of anhydrous copper sulfate, 0.8 parts of ammonium molybdate, and 300 parts of 2-ethylhexylbenzene were added to the same reactor as used in Example 1, and stirred. 7.2 parts of ε-type copper phthalocyanine crude pigment powder obtained in Example 2, formula () 7.2 parts of a compound represented by was added. 110℃ in 30 minutes
Stir at the same temperature for 30 minutes, then stir for 1 hour.
The temperature was raised to 180°C, and the mixture was further stirred at the same temperature for 4 hours.
The gas generated during the reaction was released to the outside of the system by opening the pressure regulating valve at the tip of the reflux condenser. 109 parts of copper phthalocyanine having a pure ε-type X-ray diffraction spectrum was obtained by processing in the same manner as in Example 1. BET of this pigment
The specific surface area determined by the method was 18.5 m 2 /g. Example 4 120 parts of phthalimide, 104 parts of urea, 19.7 parts of copper hydroxide, 0.8 parts of ammonium molybdate, and 150,300 parts of sorbet were added to the same reactor as used in Example 1 and stirred. Similarly obtained, ε
Completion of synthesis reaction solution containing 12 parts of type copper phthalocyanine and formula () 9.6 parts of a compound represented by was added. By operating in the same manner as in Example 3, 108 parts of copper phthalocyanine exhibiting a pure ε-type X-ray diffraction spectrum was obtained. The specific surface area of this pigment as measured by the BET method was 17.8 m 2 /g. Examples 5-10 The operation of Example 1 was repeated by changing the amounts of the crystalline modifier and the ε-type copper phthalocyanine crude pigment powder.
【表】
いずれの場合も純粋なε型のX線回折スペクト
ルを示す銅フタロシアニンが得られた。
比較例 1〜8
比較の為に、結晶系改質剤とε型銅フタロシア
ニン粗製顔料粉末を、本特許請求範囲外の量と比
率に変えて、実施例1の操作を繰り返した。[Table] In all cases, copper phthalocyanine exhibiting a pure ε-type X-ray diffraction spectrum was obtained. Comparative Examples 1-8 For comparison, the operation of Example 1 was repeated by changing the amounts and ratios of the crystalline modifier and the ε-type copper phthalocyanine crude pigment powder outside the scope of the claims.
【表】
いずれの場合も純粋なε型のX線回折スペクト
ルを示す銅フタロシアニンは得られなかつた。
参考例
実施例1で得たε型銅フタロシアニン粗製顔料
225部と粉砕した食塩1600部を双腕型ニーダーに
加え、更にジエチレングリコール230部を加えて、
80゜乃至90℃で6時間磨砕して後、熱水で洗滌し、
過して、充分水洗し、80℃で乾燥して、BET
法による比表面積68m2/gの美麗な青色の顔料
220部を得た。
この顔料2.0部を直径1mmのガラスビーズ40部
の入つたガラス瓶に入れ、メラミン―アルキツド
系焼付塗料ワニス7部とキシレン4部を加えて、
ペイントシエーカーにかけ1時間運転して後、同
じメラミン―アルキツドワニス27部を加えて10分
間更に運転して、ガラスビーズを金網でこし別
け、青の原色塗料を得た。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
で良く混合して青色塗料を作つた。
別に、塗料用として既知の方法で結晶安定化処
理を経て作られたα型銅フタロシアニンを用い
て、全く同じ方法で青色塗料を得た。この両者を
並べてガラス板上に塗布し、120℃で30分焼付け
たところ、実施例1で得られた本発明の顔料を用
いた塗料は、色相がより赤味強く、より鮮明で、
着色力も約30%高かつた。
又、実施例1の顔料1.0部を平版インキ用樹脂
ワニス1.6部とフーバーマラー上で100回転3サイ
クル練つてインキとし、比較のための無処理のα
型銅フタロシアニン顔料を用いて、同様にして得
たインキと並べて紙に展色したところ、塗料の場
合と同様、本発明による顔料を用いたインキは色
調がより赤味、鮮明で、着色力も高いという結果
を示した。[Table] In either case, copper phthalocyanine exhibiting a pure ε-type X-ray diffraction spectrum was not obtained. Reference example ε-type copper phthalocyanine crude pigment obtained in Example 1
Add 225 parts and 1600 parts of crushed common salt to a double-arm kneader, and further add 230 parts of diethylene glycol.
After grinding at 80° to 90°C for 6 hours, wash with hot water,
Wash thoroughly with water, dry at 80℃, and use BET.
Beautiful blue pigment with a specific surface area of 68m 2 /g by method
Obtained 220 copies. 2.0 parts of this pigment was placed in a glass bottle containing 40 parts of glass beads with a diameter of 1 mm, and 7 parts of melamine-alkyd baking paint varnish and 4 parts of xylene were added.
After running the paint shaker for 1 hour, 27 parts of the same melamine-alkyd varnish was added and running for another 10 minutes, and the glass beads were strained through a wire mesh to obtain a blue primary color paint. Three parts of this primary color paint and five parts of a white paint of the same type containing 30% titanium white were mixed well with a glass rod to make a blue paint. Separately, a blue paint was obtained in exactly the same manner using α-type copper phthalocyanine prepared through crystal stabilization treatment using a known method for paint use. When both were applied side by side on a glass plate and baked at 120°C for 30 minutes, the paint using the pigment of the present invention obtained in Example 1 had a more reddish hue and was clearer.
The coloring power was also approximately 30% higher. In addition, 1.0 part of the pigment of Example 1 was kneaded with 1.6 parts of resin varnish for lithographic ink on a Hubermaller for 3 cycles at 100 revolutions to make an ink, and an untreated α
When a type of copper phthalocyanine pigment was used and spread on paper next to an ink obtained in the same manner, it was found that, as in the case of paint, the ink using the pigment according to the present invention had a redder tone, clearer color, and higher coloring power. The results showed that.
第1図は、シード結晶としてのε型銅のフタロ
シアニン粗製顔料と結晶系改質剤の使用割合の変
化と、生成する銅フタロシアニンの結晶型の関連
を示す図である。
FIG. 1 is a diagram showing the relationship between changes in the proportions of an ε-type copper phthalocyanine crude pigment used as a seed crystal and a crystalline modifier, and the crystal type of the produced copper phthalocyanine.
Claims (1)
で、フタロシアニン環を形成し得る有機化合物と
尿素、銅化合物及び反応触媒を加熱撹拌して銅フ
タロシアニンを合成するに際し、次式()に示
される (式中Pcは金属或いは金属不含フタロシアニ
ン残基を表わし、Mは水素原子又はアルカリ金属
原子或いはアンモニウム基を表わし、R1,R2は
水素原子、ハロゲン原子、アルキル基、アルコキ
シ基、アルカノール基を表わし、x及びyはそれ
ぞれ0ないし4、zは1ないし4の数字を表わす
が、x,y及びzの合計は1ないし4の範囲にあ
る。) 結晶系改質剤とシード結晶としての比表面積が
35m2/g以下のε型銅フタロシアニン粗製顔料
を、フタロシアニン環を形成し得る有機化合物に
対する重量比で、結晶系改質剤の使用割合を横軸
(X)にとり、ε型銅フタロシアニン粗製顔料使
用割合を縦軸(Y)にとつた場合、点A(X=4.0
%、Y=6.0%)と点B(X=4.0%、Y=10%)
を結ぶ直線と点A(X=4.0%、Y=6.0%)と点
C(X=10%、Y=6.0%)を結ぶ直線にはさまれ
た範囲(但し、X≧4.0%、Y≧6.0%)内の量で
添加しておくことを特徴とするε型銅フタロシア
ニンの製造方法。[Claims] 1. When synthesizing copper phthalocyanine by heating and stirring an organic compound capable of forming a phthalocyanine ring, urea, a copper compound, and a reaction catalyst in an alkylbenzene solvent with a boiling point of 150 to 250°C, the following formula () shown in (In the formula, Pc represents a metal or metal-free phthalocyanine residue, M represents a hydrogen atom, an alkali metal atom, or an ammonium group, and R 1 and R 2 represent a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group, an alkanol group) , x and y each represent a number from 0 to 4, z represents a number from 1 to 4, but the sum of x, y and z is in the range from 1 to 4.) As a crystal system modifier and a seed crystal specific surface area
The weight ratio of the ε-type copper phthalocyanine crude pigment of 35 m 2 /g or less to the organic compound that can form a phthalocyanine ring, and the usage ratio of the crystalline modifier is plotted on the horizontal axis (X), and the ε-type copper phthalocyanine crude pigment is used. If the ratio is plotted on the vertical axis (Y), point A (X = 4.0
%, Y=6.0%) and point B (X=4.0%, Y=10%)
The range sandwiched between the straight line connecting point A (X=4.0%, Y=6.0%) and point C (X=10%, Y=6.0%) (however, X≧4.0%, Y≧ 6.0%) A method for producing ε-type copper phthalocyanine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3527881A JPS57149358A (en) | 1981-03-13 | 1981-03-13 | Production of epsilon type copper phthalocyanine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3527881A JPS57149358A (en) | 1981-03-13 | 1981-03-13 | Production of epsilon type copper phthalocyanine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57149358A JPS57149358A (en) | 1982-09-14 |
| JPS647108B2 true JPS647108B2 (en) | 1989-02-07 |
Family
ID=12437309
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3527881A Granted JPS57149358A (en) | 1981-03-13 | 1981-03-13 | Production of epsilon type copper phthalocyanine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57149358A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4785091A (en) * | 1986-10-31 | 1988-11-15 | Sumitomo Chemical Company, Limited | Process for producing copper phthalocyanine pigment |
| JPH0763416B2 (en) * | 1991-03-25 | 1995-07-12 | タカラベルモント株式会社 | Shampoo ball washing device in hair washing device |
| JPH04128144U (en) * | 1991-05-09 | 1992-11-24 | 大阪機工株式会社 | Cutting oil injection device for machine tools |
| US5393339A (en) * | 1994-05-11 | 1995-02-28 | Miles Inc. | Preparation of phthalocyanine pigments |
| JP2002121420A (en) * | 2000-08-07 | 2002-04-23 | Dainippon Ink & Chem Inc | Copper phthalocyanine pigment and method for producing the same |
| KR20020077947A (en) * | 2001-04-03 | 2002-10-18 | 삼협자원개발 주식회사 | Production Method of Solvent for the Synthesis of Copper Phthalocyanine |
| JP2007100008A (en) * | 2005-10-07 | 2007-04-19 | Toyo Ink Mfg Co Ltd | Method for producing ε-type phthalocyanine pigment |
| JP5205715B2 (en) * | 2006-06-16 | 2013-06-05 | 東洋インキScホールディングス株式会社 | ε-type copper phthalocyanine pigment, method for producing the same, and coloring composition using the same |
| JP5447837B2 (en) * | 2007-02-19 | 2014-03-19 | ビーエーエスエフ ソシエタス・ヨーロピア | Pigment Rot 149 Manufacturing Method |
| CN105482490B (en) * | 2015-12-07 | 2017-03-22 | 江苏双乐化工颜料有限公司 | Preparation method and application of epsilon-type phthalocyanine blue |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2742066A1 (en) * | 1976-09-21 | 1978-03-23 | Ciba Geigy Ag | COPPER PHTHALOCYANINE PIGMENT COMPOSITIONS AND PROCESS FOR THEIR PRODUCTION |
-
1981
- 1981-03-13 JP JP3527881A patent/JPS57149358A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57149358A (en) | 1982-09-14 |
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