JP3453038B2 - Fine particle composite oxide black pigment - Google Patents
Fine particle composite oxide black pigmentInfo
- Publication number
- JP3453038B2 JP3453038B2 JP4859497A JP4859497A JP3453038B2 JP 3453038 B2 JP3453038 B2 JP 3453038B2 JP 4859497 A JP4859497 A JP 4859497A JP 4859497 A JP4859497 A JP 4859497A JP 3453038 B2 JP3453038 B2 JP 3453038B2
- Authority
- JP
- Japan
- Prior art keywords
- composite oxide
- pigment
- black pigment
- oxide black
- fine particle
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0081—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound
Landscapes
- Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Organic Chemistry (AREA)
- Optical Filters (AREA)
- Ink Jet Recording Methods And Recording Media Thereof (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
- Thermal Transfer Or Thermal Recording In General (AREA)
- Developing Agents For Electrophotography (AREA)
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】本発明は微粒子複合酸化物ブ
ラック顔料に関する。
【0002】
【従来の技術】従来、複合酸化物ブラック顔料は耐熱
性、色分かれ性、耐久性等に優れた無機顔料として広く
知られ、例えば、塗料や耐熱インキの着色剤や窯業用着
色剤として幅広く使用されている。上記のブラック顔料
のなかには、Cu−Cr系、Cu−Cr−Mn系、Cu
−Mn系、Cu−Fe−Mn系等があり、基本的には2
価の銅を含み、その構造は一般にはスピネル構造をして
いる。製造方法は主として乾式法によるものであって、
原料が各成分の酸化物や炭酸塩の混合物である場合に
は、これらの混合物を焼成及び粉砕することによって製
造されている。
【0003】一方、銅を含まない複合酸化物ブラック顔
料には種類は多くなく、Co−Fe−Cr系のいわゆる
コバルトブラックが知られる程度である。その製造方法
は銅を含むブラックと同様に乾式法が主流である。その
ため、本出願人らは既に微粒子化によって、黒度、着色
力、鮮映性、発色性に優れた黒色顔料及びその製造方法
について公表している(特願平8−75373号明細
書)。しかしながら、コバルトブラック顔料は、微粒子
化すると黒度や鮮映性等は従来の乾式法に比べて著しく
改良及び向上するが、薄膜化した場合には充分な隠蔽性
或いは光の遮蔽性が得られないという欠点がある。
【0004】
【発明が解決しようとしている課題】従来、蛍光体特に
青色蛍光体と接触する可能性がある箇所における耐熱黒
色顔料には、銅を含まない顔料として、例えば、グラフ
ァイトやコバルトブラック(コバルト、クロム及び鉄か
らなる複合酸化物)等が使用されてきた。しかしなが
ら、これらの従来の黒色顔料は、色調、遮蔽性及び粒子
の大きさによる諸弊害があり、上記用途には満足できる
ものではなかった。
【0005】
【課題を解決するための手段】本発明は上記従来技術の
要望に応えるべく鋭意研究の結果、コバルト、マンガン
及び鉄の3成分からなる複合酸化物ブラック顔料を見い
出し、該顔料を湿式沈澱法で合成する際に、原料の金属
塩類の混合物を水性媒体中でアルカリ剤によって中和及
び混合析出し、この析出物を析出と同時又は析出後に液
相酸化処理することにより、黒度、着色力、鮮映性及び
発色性に優れた微粒子複合酸化物ブラック顔料が得られ
ることを確認し、本発明を完成した。
【0006】即ち、本発明は、各金属の塩類の混合水溶
液から湿式沈澱法で析出させた混合析出物を液相酸化処
理し、次いで酸化性雰囲気下で焼成してなるコバルト、
マンガン及び鉄の酸化物からなり、コバルト、マンガン
及び鉄のモル比が1:1.4〜1.6:0.2〜0.6
であり、Coと(Mn+Fe)のモル比が1:1.9〜
2.1で、BET比表面積が30m 2 /g以上100m 2
/g以下であることを特徴とする微粒子複合酸化物ブラ
ック顔料である。本発明によれば、微粒子複合酸化物ブ
ラック顔料を構成する金属の塩をアルカリ沈澱剤によ
り、それら金属の水酸化物として混合析出させ、この析
出物を析出と同時又は析出後に液相中で酸化処理をする
ことにより、その後の焼成温度を極めて低くすることが
可能になり、微粒子状で、且つ黒度、着色力及び鮮映性
に優れた微粒子複合酸化物ブラック顔料が得られる。更
に該ブラック顔料は、非常に微粒子にも拘わらず、ソフ
トで分散性にも優れている。
【0007】
【発明の実施の形態】次に好ましい実施の形態を挙げて
本発明を更に詳しく説明する。本発明で使用する構成元
素の塩は、コバルト、マンガン及び鉄の硫酸塩、硝酸
塩、塩化物、酢酸塩等、従来の複合酸化物ブラック顔料
を製造するときに使用されている塩類は全て使用するこ
とができる。
【0008】本発明の顔料の原料である塩類において、
各成分の構成割合は、金属のモル比でコバルト:マンガ
ン:鉄が、1:1.4〜1.6:0.2〜0.6であ
り、最も好ましくは1:1.6:0.4の比率である。
又、Co/(Mn+Fe)が1/1.9〜2.1が好ま
しく、1/2であることが最良である。又、マンガンと
鉄の比は9/1から3/2の範囲において変化させても
得られる顔料の品質上大きな差はない。コバルト、マン
ガン及び鉄の比が上記範囲を外れたり、マンガンと鉄と
の比が上記の範囲を外れると、得られる顔料の黒度等が
低下する。
【0009】本発明の製造方法においては、以上の如き
各構成元素の必要金属塩を、水に溶かして混合塩水溶液
を形成する。その際の金属塩の濃度は上記の如きモル比
で全体として約5〜50重量%程度の濃度とするのが適
当である。この混合溶液は沈澱剤としてカセイソーダ等
のアルカリ水溶液を用いて、予め用意した沈澱媒体中に
同時に滴下される。この際の反応濃度は沈澱生成物に対
して特に悪い影響を及ぼすという程ではないが、作業性
及びその後の酸化工程等を考えると、好ましくは0.0
5モル/リットル〜0.2モル/リットルが適当であ
り、傾向としては濃度の薄い方が生成する粒子が小さく
なる。
【0010】又、上記の顔料の合成温度は通常行う範
囲、即ち0℃〜100℃の範囲であれば、その効果を十
分発揮することができる。しかしながら、合成温度が5
0℃以上では生成する粒子の成長が大きく、得られる顔
料の着色力がやや損なわれる傾向にある。又、この際の
合成時のpHは8以上のアルカリ側であれば、いずれの
pH領域でも大きくは影響しない。しかしながら、一般
的傾向として、低いpHでは粒子が大きくなる傾向があ
り、又、pHが高くなると小さな粒子が得られやすい。
【0011】そのために、顔料合成時のpHは、その後
の生成物の扱いやすさ、又、最終生成物である顔料の黒
度及び着色力に微妙に関係する。過剰のアルカリは沈澱
生成後に加えられる。この際のアルカリ過剰量は沈澱に
必要なアルカリモル数に対して1.1〜1.5倍の範
囲、望ましくは1.1倍前後が、得られる顔料の黒度及
び着色力共に最も良好である。このようにして30分間
〜1時間かけて撹拌しながら沈澱を生成させた後、5〜
20分間程度熟成を行い沈澱反応を完了させる。
【0012】次に上記で生成された共沈物中の2価の金
属イオンを3価の金属イオンに酸化することが必要であ
る。使用する酸化剤としては、過酸化水素、空気(酸
素)、塩素酸ナトリウム、過硫酸アンモニウム等、いず
れの酸化剤でもよいが、好ましい酸化剤は、酸化によっ
て不純物を生じない酸化剤、例えば、過酸化水素、空気
(酸素)が好ましい。酸化剤の使用量は、2価の金属が
3価の金属イオンに酸化されるに必要な量であればよい
が、酸化を完結するためにある程度過剰に加えるのが好
ましい。
【0013】しかしながら、上記金属の酸化反応は液の
温度、酸化剤の濃度、添加速度、アルカリ度及び液の撹
拌状態等によって、その効率が異なるため、好ましくは
酸化還元電位を測定しながら酸化剤の量を制御するのが
適当である。即ち、本条件下では酸化反応開始時、+5
00〜+600mVである電位が、反応終了時には+5
0mV〜0mVに低下する。
【0014】次に、得られた生成物を水洗及び濾過し、
100℃〜120℃程度の温度で乾燥する。得られた乾
燥物を酸化性雰囲気下で450℃〜550℃の温度で3
0分間〜1時間焼成することにより、本発明の微粒子複
合酸化物ブラック顔料を得ることができる。
【0015】このようにして得られた本発明の微粒子複
合酸化物ブラック顔料は、従来の乾式法における同一組
成の顔料に比べて、黒度、着色力及び鮮映性に優れ、B
ET比表面積を30〜100m2/gに調整すること
で、粒子の大きさを整え、塗料系への分散も良好にな
る。
【0016】
【実施例】次に実施例及び比較例を挙げて本発明を更に
具体的に説明する。尚、文中部又は%とあるのは特に断
りのない限り重量基準である。
【0017】実施例1
塩化コバルト190.4部、硫酸第一鉄7水塩136.
0部及び硫酸マンガン1水塩189.2部を計りとり、
これらを水を加えて完全に溶かして全体を約1,000
部とする。次に沈澱剤としてカセイソーダ224部を計
りとり、水を加えて約1,000部とする。
【0018】予め用意しておいた沈澱媒体である水約
2,000部をガスバーナーや電熱器等で約25℃の温
度に調整し、ここに混合塩水溶液とカセイソーダ水溶液
とを同時に滴下し、約30分間から1時間かけて沈澱反
応を完了させる。この際のpHは11前後位になるよう
に注意し、混合塩水溶液の滴下が終了したら過剰のカセ
イソーダ水溶液の滴下を続ける。滴下が終了したらpH
を保持したまま、過酸化水素水(濃度35%)100部
を水100部に希釈した溶液を滴下して酸化処理を行
う。この際の酸化反応が完全に行われたか否かは酸化還
元電位を測定しながら確認する。
【0019】次に酸化処理終了後、液温を70℃に上昇
させ1時間程度熟成を行う。こうして得られた生成物を
十分に水洗し残塩を洗い流して濾過を行う。次いで10
0℃〜120℃の温度にて12時間以上乾燥させる。こ
の乾燥物を500℃で1時間酸化雰囲気にて焼成後冷却
した。
【0020】このようにして得られた顔料は粒子が細か
く、BET比表面積が65m2/gであった。この微粒
子複合酸化物ブラック顔料をペイントコンディショナー
(レッドデビル社製)でメラミン/アルキッド樹脂(P
HR30)にて充分分散させる。そして黒帯付のアート
紙に3ミルのアプリケーターにて展色し色調を観察し
た。又、透明PETフィルム上にも展色し、光の透過率
を観察した。更に酸化チタンで薄めたものについて着色
力を観察した。
【0021】その結果、この微粒子複合酸化物顔料は黒
度が高く、鮮映性に優れ、着色力も高く、薄膜化した場
合の光の遮蔽性も高く、且つ分散性も良好な微粒子複合
酸化物ブラック顔料であった。
【0022】比較例1
塩化コバルト57.1重量部、硫酸第一鉄62.5重量
部及び40%硫酸クロム溶液125重量部を計りとり、
水を加えて約500重量部とする。次に沈澱剤としてカ
セイソーダ69重量部を計りとり、水を加えて500重
量部とする。
【0023】予め用意しておいた沈澱媒体である水約
1,000部をガスバーナーや電熱器等で約25℃の温
度に調整し、ここに混合水溶液とカセイソーダ水溶液と
を同時に滴下し、約30分間から1時間かけて沈澱反応
を完了させる。この際のpHは11前後になるように注
意し、混合塩水溶液の滴下が終了したら過剰のカセイソ
ーダを続けて加えた後、20分間程熟成する。
【0024】次ぎに、先の細いキャピラリー状に加工し
たガラス管を用意し、上記沈澱生成物の底部から1.2
リットル/min.流量の空気を吹き込む。この間、撹
拌は続けて行い、撹拌羽根の回転速度は300rpm前
後、温度は25℃に調節し、空気吹き込みは約3時間続
けた。最初の緑味の灰色沈澱物は終わりには赤み茶色沈
澱物に変化する。
【0025】次ぎに、生成物を取り出しデカンテーショ
ンにより充分に水洗し、残塩を洗い流し、濾過を行う。
次いで100〜120℃の温度にて12時間以上乾燥さ
せる。この乾燥物を700℃で1時間酸化雰囲気にて焼
成後冷却した。このようにして得られた顔料は実施例1
と同様な方法にて色調、透過性及び分散性等を観察し
た。以上の結果をまとめて表1に示す。
【0026】
【表1】※色相、鮮映性、分散性:メラミンアルキッド/PHR
30にて観察。
※透過率:上記塗料をPETフィルム上に塗布後可視部
の透過率測定値。
【0027】
【発明の効果】以上の通り、本発明によれば、粒子径が
小さく、且つ黒度、着色力及び鮮映性に優れた微粒子複
合酸化物ブラック顔料が得られ、該顔料は従来の顔料と
同様に一般の塗料、建材用着色剤や合成樹脂の着色剤、
窯業用着色剤として使用されるとともに、顔料を微粒子
化することによって新たに発現する特性を利用して、例
えば、カラーフィルター等のブラックマトリックス用ブ
ラック顔料、インクジェット用ブラック顔料、特殊塗料
用ブラック顔料等として有用である。
【0028】更に本発明の顔料は、構成元素に銅を含ま
ないため、蛍光体との接触の危険性のある蛍光表示管、
CRTディスプレイ、プラズマディスプレイ等のブラッ
クマトリックス用ブラック顔料、更には透過率、明度及
び外光反射調整用ブラック顔料等としても有用である。BACKGROUND OF THE INVENTION [0001] [Technical Field of the Invention The present invention relates to the fine composite oxide black face charges. [0002] Hitherto, composite oxide black pigments have been widely known as inorganic pigments having excellent heat resistance, color separation properties, durability and the like, and include, for example, colorants for paints and heat-resistant inks and colorants for the ceramic industry. Widely used as. Among the above black pigments, Cu-Cr-based, Cu-Cr-Mn-based, Cu
-Mn-based, Cu-Fe-Mn-based and the like.
It contains copper of the valency, and the structure generally has a spinel structure. The production method is mainly by the dry method,
When the raw material is a mixture of oxides and carbonates of each component, the mixture is produced by firing and pulverizing the mixture. On the other hand, the composite oxide black pigment containing no copper type is not large, is the degree to which C o -Fe-Cr system called cobalt black is known. As for the production method, a dry method is mainly used like black containing copper. For this reason, the present applicants have already disclosed a black pigment excellent in blackness, coloring power, sharpness and color development by making fine particles and a method for producing the same (Japanese Patent Application No. 8-75373). However, when the cobalt black pigment is finely divided, the degree of blackness and sharpness are remarkably improved and improved as compared with the conventional dry method, but when the pigment is formed into a thin film, sufficient concealing properties or light shielding properties are obtained. There is a disadvantage that there is no. [0004] Conventionally, heat-resistant black pigments at locations that may come into contact with a phosphor, particularly a blue phosphor, include, as pigments not containing copper, for example, graphite and cobalt black (cobalt black). Chromium and iron). However, these conventional black pigments have various harmful effects due to color tone, shielding property and particle size, and have not been satisfactory for the above-mentioned applications. In order to meet the demands of the prior art, the present invention has conducted intensive studies, and as a result, has found a composite oxide black pigment composed of three components of cobalt, manganese and iron, and wet-processed the pigment. When synthesizing by the precipitation method, the mixture of the raw material metal salts is neutralized and mixed and precipitated by an alkali agent in an aqueous medium, and the precipitates are subjected to liquid phase oxidation treatment simultaneously with or after the precipitation, whereby blackness, It has been confirmed that a fine particle composite oxide black pigment excellent in tinting strength, sharpness and color development can be obtained, and the present invention has been completed. That is, the present invention relates to a mixed aqueous solution of salts of each metal.
The mixed precipitate deposited from the liquid by wet precipitation is subjected to a liquid phase oxidation treatment.
And then calcined in an oxidizing atmosphere ,
Ri Do oxides of manganese and iron, cobalt, manganese
And the molar ratio of iron is 1: 1.4 to 1.6: 0.2 to 0.6.
And the molar ratio of Co to (Mn + Fe) is 1: 1.9 to
2.1, BET specific surface area of 30 m 2 / g or more and 100 m 2
/ A particulate composite oxide black Pigment, characterized in that g or less. According to the present invention, a salt of a metal constituting the particulate composite oxide black pigment is mixed and precipitated as a hydroxide of the metal with an alkaline precipitant, and the precipitate is oxidized in a liquid phase simultaneously with or after the precipitation. By performing the treatment, the subsequent firing temperature can be extremely reduced, and a fine-particle composite oxide black pigment excellent in blackness, coloring power and sharpness can be obtained. Further, the black pigment is soft and excellent in dispersibility despite being very fine. Next, the present invention will be described in more detail by way of preferred embodiments. As the salts of the constituent elements used in the present invention, all salts used when producing conventional complex oxide black pigments, such as sulfates, nitrates, chlorides, acetates of cobalt, manganese and iron, are used. be able to. In the salts which are the raw materials of the pigment of the present invention,
The composition ratio of each component is such that the molar ratio of cobalt: manganese: iron is 1: 1.4 to 1.6 : 0.2 to 0.6, most preferably 1: 1.6: 0. The ratio is 4.
Further, Co / (Mn + Fe) is preferably 1 / 1.9 to 2.1, and most preferably 1/2. Even if the ratio of manganese to iron is changed in the range of 9/1 to 3/2, there is no significant difference in the quality of the obtained pigment. When the ratio of cobalt, manganese, and iron is out of the above range, or the ratio of manganese to iron is out of the above range, the blackness and the like of the obtained pigment is reduced. In the production method of the present invention, the required metal salts of the respective constituent elements as described above are dissolved in water to form a mixed salt aqueous solution. The concentration of the metal salt at that time is suitably about 5 to 50% by weight as a whole in the above molar ratio. This mixed solution is simultaneously dropped into a previously prepared precipitating medium using an aqueous alkaline solution such as caustic soda as a precipitating agent. The reaction concentration at this time is not so great as to have a particularly bad influence on the precipitated product, but is preferably 0.00 in consideration of workability and the subsequent oxidation step.
5 mol / l to 0.2 mol / l is appropriate, and the lower the concentration, the smaller the generated particles. [0010] If the synthesis temperature of the above-mentioned pigment is within the usual range, that is, within the range of 0 ° C to 100 ° C, the effect can be sufficiently exhibited. However, if the synthesis temperature is 5
If the temperature is 0 ° C. or higher, the generated particles grow greatly, and the coloring power of the obtained pigment tends to be slightly impaired. In addition, as long as the pH at the time of synthesis at this time is on the alkaline side of 8 or more, there is no significant effect in any pH range. However, as a general tendency, particles tend to be large at low pH, and small particles tend to be obtained at high pH. For this reason, the pH at the time of the synthesis of the pigment is delicately related to the ease of handling of the subsequent product and the blackness and coloring power of the final product pigment. Excess alkali is added after precipitation. At this time, the excess amount of alkali is in the range of 1.1 to 1.5 times, preferably about 1.1 times, the number of moles of alkali required for precipitation, and the obtained pigment has the best blackness and coloring power. is there. After forming a precipitate while stirring for 30 minutes to 1 hour,
Aging is performed for about 20 minutes to complete the precipitation reaction. Next, it is necessary to oxidize the divalent metal ions in the coprecipitate generated above into trivalent metal ions. The oxidizing agent to be used may be any oxidizing agent such as hydrogen peroxide, air (oxygen), sodium chlorate, ammonium persulfate, etc. A preferable oxidizing agent is an oxidizing agent which does not generate impurities by oxidation, for example, peroxide Hydrogen and air (oxygen) are preferred. The amount of the oxidizing agent used may be an amount necessary to oxidize a divalent metal to a trivalent metal ion, but it is preferable to add the oxidizing agent in a certain amount to complete the oxidation. However, the efficiency of the metal oxidation reaction varies depending on the temperature of the liquid, the concentration of the oxidizing agent, the rate of addition, the alkalinity, the stirring state of the liquid, and the like. Is suitably controlled. That is, under this condition, at the start of the oxidation reaction, +5
A potential of 00 to +600 mV is +5 at the end of the reaction.
It falls to 0 mV to 0 mV. Next, the obtained product is washed with water and filtered,
Dry at a temperature of about 100C to 120C. The resulting dried product in an oxidizing atmosphere 3 at a temperature of 450 ° C. to 5 5 0 ° C.
By baking for 0 minute to 1 hour, the fine particle composite oxide black pigment of the present invention can be obtained. [0015] The fine particle composite oxide black pigment of the present invention thus obtained is excellent in blackness, coloring power and sharpness as compared with pigments having the same composition in a conventional dry method, and
By adjusting the ET specific surface area to 30 to 100 m 2 / g, the size of the particles is adjusted, and the dispersion in the coating system becomes good. The present invention will now be described more specifically with reference to examples and comparative examples. In the following, "parts" and "%" are based on weight unless otherwise specified. Example 1 190.4 parts of cobalt chloride, ferrous sulfate heptahydrate
Weigh out 0 parts and 189.2 parts of manganese sulfate monohydrate,
These are completely dissolved by adding water, and the whole is about 1,000
Department. Next, 224 parts of caustic soda is measured as a precipitant, and water is added to make about 1,000 parts. About 2,000 parts of water as a precipitating medium prepared in advance is adjusted to a temperature of about 25 ° C. with a gas burner, an electric heater, or the like, and an aqueous mixed salt solution and an aqueous caustic soda solution are simultaneously dropped therein, The precipitation reaction is completed in about 30 minutes to 1 hour. At this time, care is taken so that the pH is about 11, and when the dropwise addition of the mixed salt aqueous solution is completed, the excess sodium hydroxide aqueous solution is continuously added dropwise. PH after dropping
While maintaining the above, a solution obtained by diluting 100 parts of a hydrogen peroxide solution (concentration: 35%) into 100 parts of water is dropped to perform an oxidation treatment. Whether or not the oxidation reaction at this time has been completed is confirmed by measuring the oxidation-reduction potential. Next, after the completion of the oxidation treatment, the liquid temperature is raised to 70 ° C. and aging is performed for about one hour. The product thus obtained is thoroughly washed with water to remove residual salts and filtered. Then 10
Dry at a temperature of 0 ° C to 120 ° C for 12 hours or more. The dried product was fired at 500 ° C. for 1 hour in an oxidizing atmosphere and then cooled. The pigment thus obtained had fine particles and a BET specific surface area of 65 m 2 / g. This fine particle composite oxide black pigment is applied to a melamine / alkyd resin (P) with a paint conditioner (manufactured by Red Devil Co., Ltd.).
HR30). The color was then applied to art paper with a black belt using a 3 mil applicator, and the color tone was observed. Further, the color was spread on the transparent PET film, and the light transmittance was observed. Further, the coloring power of the titanium oxide thinner was observed. As a result, the fine particle composite oxide pigment has high blackness, excellent image clarity, high coloring power, high light shielding property when thinned, and good dispersibility. It was a black pigment. Comparative Example 1 57.1 parts by weight of cobalt chloride, 62.5 parts by weight of ferrous sulfate and 125 parts by weight of a 40% chromium sulfate solution were weighed out.
Add water to make about 500 parts by weight. Next, 69 parts by weight of caustic soda is measured as a precipitant, and water is added to make up to 500 parts by weight. About 1,000 parts of water, which is a precipitating medium, prepared in advance is adjusted to a temperature of about 25 ° C. with a gas burner, an electric heater, or the like, and a mixed aqueous solution and an aqueous caustic soda solution are simultaneously dripped thereto. The precipitation reaction is completed in 30 minutes to 1 hour. At this time, care is taken so that the pH is about 11. When dripping of the mixed salt aqueous solution is completed, excess caustic soda is continuously added, followed by aging for about 20 minutes. Next, a glass tube processed into a thin capillary was prepared, and 1.2 g from the bottom of the precipitated product was prepared.
Liter / min. Blow in air at the flow rate. During this time, stirring was continued, the rotation speed of the stirring blade was adjusted to about 300 rpm, the temperature was adjusted to 25 ° C., and air blowing was continued for about 3 hours. The initial greenish gray precipitate changes to a reddish brown precipitate at the end. Next, the product is taken out and sufficiently washed with decantation to remove residual salts, followed by filtration.
Next, it is dried at a temperature of 100 to 120 ° C. for 12 hours or more. This dried product was fired at 700 ° C. for 1 hour in an oxidizing atmosphere and then cooled. The pigment thus obtained was prepared in Example 1.
The color tone, transmittance, dispersibility and the like were observed in the same manner as in the above. Table 1 summarizes the above results. [Table 1] * Hue, sharpness, dispersibility: Melamine alkyd / PHR
Observed at 30. * Transmittance: The measured transmittance of the visible part after the above coating material was applied on a PET film. As described above, according to the present invention, a fine particle composite oxide black pigment having a small particle diameter and excellent in blackness, coloring power and sharpness can be obtained. Similar to general pigments, general paints, colorants for building materials and colorants for synthetic resins,
It is used as a colorant for the ceramic industry, and utilizes the properties newly developed by making the pigment into fine particles. For example, black pigments for black matrices such as color filters, black pigments for inkjets, black pigments for special paints, etc. Useful as Further, since the pigment of the present invention does not contain copper as a constituent element, there is a danger of contact with a fluorescent substance in a fluorescent display tube.
It is also useful as a black pigment for a black matrix such as a CRT display and a plasma display, as well as a black pigment for adjusting transmittance, brightness and external light reflection.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI G03G 9/09 G03G 9/08 361 (72)発明者 寺田 裕美 東京都中央区日本橋馬喰町1−7−6 大日精化工業株式会社内 (72)発明者 川上 徹 東京都中央区日本橋馬喰町1−7−6 大日精化工業株式会社内 (56)参考文献 特開 昭49−124127(JP,A) 特開 昭53−81536(JP,A) 特開 昭59−147414(JP,A) 特開 昭59−138312(JP,A) 特開 平9−12768(JP,A) 特開 平9−25126(JP,A) 特開 平4−50119(JP,A) (58)調査した分野(Int.Cl.7,DB名) C09C 1/00 - 3/12 C01G 45/00 - 45/10 C01G 49/00 - 51/12 B41M 5/00 - 5/26 G03G 9/08 G02G 5/22 ────────────────────────────────────────────────── ─── Continued on the front page (51) Int.Cl. 7 Identification symbol FI G03G 9/09 G03G 9/08 361 (72) Inventor Hiromi Terada 1-7-6 Nihombashi Bakurocho, Chuo-ku, Tokyo Dainichi Seika Kogyo Co., Ltd. In-company (72) Inventor Toru Kawakami 1-6-6 Bakurocho, Nihonbashi, Chuo-ku, Tokyo Inside Dainichi Seika Industry Co., Ltd. (56) References JP-A-49-124127 (JP, A) JP-A-53-81536 ( JP, A) JP-A-59-147414 (JP, A) JP-A-59-138312 (JP, A) JP-A-9-12768 (JP, A) JP-A-9-25126 (JP, A) Hei 4-50119 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C09C 1/00-3/12 C01G 45/00-45/10 C01G 49/00-51/12 B41M 5/00-5/26 G03G 9/08 G02G 5/22
Claims (1)
法で析出させた混合析出物を液相酸化処理し、次いで酸
化性雰囲気下で焼成してなるコバルト、マンガン及び鉄
の酸化物からなり、コバルト、マンガン及び鉄のモル比
が1:1.4〜1.6:0.2〜0.6であり、Coと
(Mn+Fe)のモル比が1:1.9〜2.1で、BE
T比表面積が30m 2 /g以上100m 2 /g以下である
ことを特徴とする微粒子複合酸化物ブラック顔料。(57) [Claims 1] Wet precipitation from a mixed aqueous solution of salts of each metal
The mixed precipitate deposited by the method is subjected to liquid phase oxidation treatment,
Cobalt made by firing under a reduction atmosphere, Ri Do oxides of manganese and iron, cobalt, the molar ratio of manganese and iron
Is 1: 1.4 to 1.6: 0.2 to 0.6, and Co and
When the molar ratio of (Mn + Fe) is 1: 1.9 to 2.1, BE
A fine particle composite oxide black pigment having a T specific surface area of 30 m 2 / g or more and 100 m 2 / g or less .
Priority Applications (1)
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JP4859497A JP3453038B2 (en) | 1997-02-18 | 1997-02-18 | Fine particle composite oxide black pigment |
Applications Claiming Priority (1)
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JP4859497A JP3453038B2 (en) | 1997-02-18 | 1997-02-18 | Fine particle composite oxide black pigment |
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JPH10231441A JPH10231441A (en) | 1998-09-02 |
JP3453038B2 true JP3453038B2 (en) | 2003-10-06 |
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US7465495B2 (en) | 2003-10-15 | 2008-12-16 | Mitsu Mining & Smelting Co., Ltd. | Composite black oxide particle, method for producing same, black coating material and black matrix |
JP4495995B2 (en) * | 2004-03-31 | 2010-07-07 | 三井金属鉱業株式会社 | Method for producing composite black oxide particles, black paint and black matrix |
JP2006056184A (en) | 2004-08-23 | 2006-03-02 | Konica Minolta Medical & Graphic Inc | Printing plate material and printing plate |
JP2006088614A (en) | 2004-09-27 | 2006-04-06 | Konica Minolta Medical & Graphic Inc | Printing plate material |
JP4682074B2 (en) * | 2005-03-31 | 2011-05-11 | 三井金属鉱業株式会社 | Composite oxide particles exhibiting black color |
JP4688708B2 (en) * | 2005-04-01 | 2011-05-25 | 三井金属鉱業株式会社 | Black composite oxide particles, production method thereof, black paste and black matrix |
KR101246150B1 (en) | 2005-04-01 | 2013-03-25 | 미쓰이금속광업주식회사 | Black double oxide particles, process for production thereof, black pastes, and black matrixes |
US7615581B2 (en) * | 2005-08-17 | 2009-11-10 | Lg Electronics Inc. | Black paste composite, upper plate of plasma display panel, and manufacturing method by using the same |
CN101316721A (en) | 2005-11-01 | 2008-12-03 | 柯尼卡美能达医疗印刷器材株式会社 | Lithographic printing plate material, lithographic printing plate, method for preparing lithographic printing plate, and method for printing by lithographic printing plate |
JP4682072B2 (en) * | 2006-03-24 | 2011-05-11 | 三井金属鉱業株式会社 | Black composite oxide particles, production method thereof, black slurry, black paste, and black matrix |
JP6331983B2 (en) * | 2014-11-12 | 2018-05-30 | 住友金属鉱山株式会社 | Method for producing transition metal composite hydroxide particles and method for producing positive electrode active material for non-aqueous electrolyte secondary battery |
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