JP4563065B2 - Dispersant for inorganic pigment - Google Patents

Dispersant for inorganic pigment Download PDF

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JP4563065B2
JP4563065B2 JP2004106157A JP2004106157A JP4563065B2 JP 4563065 B2 JP4563065 B2 JP 4563065B2 JP 2004106157 A JP2004106157 A JP 2004106157A JP 2004106157 A JP2004106157 A JP 2004106157A JP 4563065 B2 JP4563065 B2 JP 4563065B2
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JP2005290165A (en
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洋一 石橋
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Kao Corp
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Description

本発明は、無機顔料を水等に分散させてスラリーを得る際に好適に用いられる無機顔料用分散剤及びそれを含有する顔料分散組成物に関する。   The present invention relates to an inorganic pigment dispersant suitably used when an inorganic pigment is dispersed in water or the like to obtain a slurry, and a pigment dispersion composition containing the dispersant.

無機顔料を水系媒体中に分散し、スラリー化するに際しては、ポリカルボン酸塩系分散剤が使用されている。例えば、アクリル酸とマレイン酸との共重合体の塩が知られているが、スラリーの高濃度化に伴い、十分な分散性能が得られなくなってきている。   In dispersing an inorganic pigment in an aqueous medium to form a slurry, a polycarboxylate-based dispersant is used. For example, a salt of a copolymer of acrylic acid and maleic acid is known, but as the concentration of the slurry is increased, sufficient dispersion performance cannot be obtained.

特許文献1ではアクリル酸とマレイン酸との共重合モル比の異なる2種の共重合体の組み合わせにより分散性能の向上を報告している。しかしながら例えば水性塗料用途等で無機顔料スラリーをスプレーのようにシェア(剪断)のかかる状態で塗布する場合と、ハケのようにシェアのかからない状態で塗布する場合、スラリー粘度が大きく異なり(チキソトロピー性が大きい)、作業性に支障を及ぼす点が指摘されていた。
特開平8−188986号公報
Patent Document 1 reports an improvement in dispersion performance by a combination of two kinds of copolymers having different copolymerization molar ratios of acrylic acid and maleic acid. However, for example, when the inorganic pigment slurry is applied in a state where shear (shear) is applied like spray for application in water-based paint, etc., the slurry viscosity is greatly different (thixotropic property is different). It was pointed out that it would interfere with workability.
JP-A-8-188986

本発明の課題は、シェアの影響による無機顔料スラリー粘度の変化が小さく、また粘度値も低くすることができる無機顔料用分散剤及びそれを含有する顔料分散組成物を提供することにある。   An object of the present invention is to provide a dispersant for an inorganic pigment that can change the viscosity of the inorganic pigment slurry due to the influence of the share and can also reduce the viscosity value, and a pigment dispersion composition containing the dispersant.

本発明は、下記の(A)成分及び(B)成分を、(A)/(B)=50/50〜96/4(重量比)の割合で含有する無機顔料用分散剤、及びこの無機顔料用分散剤を含有する顔料分散組成物を提供する。
(A)成分:
構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=91/9〜74/26で、重量平均分子量(Mw)が25000〜60000である、不飽和一塩基酸と不飽和二塩基酸との共重合体の塩
(B)成分:
構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=63/37〜47/53で、重量平均分子量(Mw)が25000〜60000である、不飽和一塩基酸と不飽和二塩基酸との共重合体の塩
The present invention provides an inorganic pigment dispersant containing the following components (A) and (B) in a ratio of (A) / (B) = 50/50 to 96/4 (weight ratio), and the inorganic Provided is a pigment dispersion composition containing a pigment dispersant.
(A) component:
An unsaturated monobasic acid having a constituent monomer unit ratio of unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 91/9 to 74/26 and a weight average molecular weight (Mw) of 25,000 to 60,000 Salt (B) component of copolymer with unsaturated dibasic acid:
An unsaturated monobasic acid having a constituent monomer unit ratio of unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 63/37 to 47/53 and a weight average molecular weight (Mw) of 25,000 to 60,000 Salts of copolymers with unsaturated dibasic acids

本発明の無機顔料用分散剤は、シェアの影響による無機顔料スラリー粘度の変化が小さく、また粘度値も低くすることができる。   The inorganic pigment dispersant of the present invention has a small change in the viscosity of the inorganic pigment slurry due to the influence of the shear, and can also have a low viscosity value.

本発明の(A)成分、(B)成分それぞれの共重合体を構成する不飽和一塩基酸としては、アクリル酸、メタクリル酸、クロトン酸等が挙げられるが、アクリル酸、メタクリル酸が好ましい。また、不飽和二塩基酸としては、マレイン酸無水物、マレイン酸、イタコン酸、フマル酸等が挙げられるが、マレイン酸無水物、マレイン酸、イタコン酸が好ましい。   Examples of the unsaturated monobasic acid constituting the copolymer of each of the components (A) and (B) of the present invention include acrylic acid, methacrylic acid, crotonic acid and the like, but acrylic acid and methacrylic acid are preferred. Examples of the unsaturated dibasic acid include maleic anhydride, maleic acid, itaconic acid, fumaric acid and the like, and maleic anhydride, maleic acid and itaconic acid are preferred.

本発明の(A)成分、(B)成分それぞれの共重合体の塩としては、アルカリ金属塩、アルカリ土類金属塩、4級アンモニウム塩、アンモニウム塩、有機アミン塩から選ばれる少なくとも1種が好ましい。   The salt of the copolymer of each of the component (A) and the component (B) of the present invention is at least one selected from alkali metal salts, alkaline earth metal salts, quaternary ammonium salts, ammonium salts, and organic amine salts. preferable.

塩を構成するアルカリ金属としては、ナトリウム、カリウム、リチウム等が挙げられる。アルカリ土類金属としては、マグネシウム、カルシウム、バリウム等が挙げられる。4級アンモニウムとしては、水酸化テトラメチルアンモニウム、水酸化トリエチルメチルアンモニウム等が挙げられる。有機アミンとしては、ジエタノールアミン、トリエタノールアミン、エチレンジアミン、ジエチレントリアミン、トリエチルアミン、トリブチルアミン等が挙げられる。   Examples of the alkali metal constituting the salt include sodium, potassium, and lithium. Examples of the alkaline earth metal include magnesium, calcium, and barium. Examples of the quaternary ammonium include tetramethylammonium hydroxide and triethylmethylammonium hydroxide. Examples of the organic amine include diethanolamine, triethanolamine, ethylenediamine, diethylenetriamine, triethylamine, and tributylamine.

これらの中で好ましいものは、顔料の高濃度スラリーを低粘度化し、低粘度化スラリーを長期分散安定化する観点において、アルカリ金属塩であり、ナトリウム塩、カリウム塩がより好ましい。また、アンモニウム塩は電子材料等の灰分の残存を嫌う用途への使用に好ましい。   Among these, preferred are alkali metal salts, and sodium salts and potassium salts are more preferable from the viewpoint of lowering the viscosity of a high-concentration slurry of pigment and stabilizing the low-viscosity slurry for a long period of time. Ammonium salts are preferred for use in applications where ash content remains, such as electronic materials.

本発明の(A)成分、(B)成分それぞれの共重合体の塩の中和度又はアルカリ過剰度は、特に規定されないが、粉体成分の耐分解性、並びに耐着色性及び耐臭気性の観点から、通常それぞれ50〜120%であり、60〜110%が好ましく、75〜105%がより好ましい。   The degree of neutralization or alkali excess of the salt of the copolymer of each of the components (A) and (B) of the present invention is not particularly defined, but the decomposition resistance, color resistance and odor resistance of the powder component In view of the above, it is usually 50 to 120%, preferably 60 to 110%, more preferably 75 to 105%.

尚、中和度又はアルカリ過剰度とは、[A(塩を構成し得るフリーの塩基の当量+塩を構成している酸基の当量)/B(塩を構成し得るフリーの酸基の当量+塩を構成している酸基の当量)]×100(%)で表される。A/Bが1以下であれば中和度と表現し、A/B=1であれば中和度100%を示す。A/Bが1より大きいものはアルカリ過剰度と表現し、100%より大きい値を示す。   The degree of neutralization or the excess of alkali means [A (equivalent of free base capable of constituting a salt + equivalent of acid group constituting a salt) / B (free acid group capable of constituting a salt). Equivalent + equivalent of acid group constituting the salt)] × 100 (%). When A / B is 1 or less, the degree of neutralization is expressed, and when A / B = 1, the degree of neutralization is 100%. A / B greater than 1 is expressed as alkali excess and shows a value greater than 100%.

また、(A)成分、(B)成分それぞれの共重合体の塩の水溶液のpHは、粉体成分の耐分解性、並びに耐着色性及び耐臭気性の観点から、5〜9が好ましく、5.5〜8.5が更に好ましく、6〜8が特に好ましい。   Moreover, the pH of the aqueous solution of the copolymer salt of each of the component (A) and the component (B) is preferably 5 to 9 from the viewpoint of the decomposition resistance of the powder component, and the resistance to coloring and odor. 5.5 to 8.5 is more preferable, and 6 to 8 is particularly preferable.

本発明の(A)成分は、構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=91/9〜74/26であり、91/9〜80/20が好ましく、87/13〜80/20が更に好ましい。   In the component (A) of the present invention, the constituent monomer unit ratio is unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 91/9 to 74/26, preferably 91/9 to 80/20. 87/13 to 80/20 are more preferable.

また、本発明の(B)成分は、構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=63/37〜47/53であり、61/39〜48/52が好ましく、59/41〜50/50が更に好ましい。   In addition, the component (B) component of the present invention has a constituent monomer unit ratio of unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 63/37 to 47/53, and 61/39 to 48/52. Is preferable, and 59/41 to 50/50 is more preferable.

本発明の(A)成分、(B)成分それぞれの重量平均分子量(Mw)は、顔料の高濃度スラリーを低粘度化し、低粘度化スラリーを長期分散安定化し、高剪断下におけるスラリーの粘度を小さく維持する観点から、25000〜60000であり、35000〜50000が好ましく、40000〜50000が更に好ましい。   The weight average molecular weight (Mw) of each of the component (A) and the component (B) of the present invention is such that the high-concentration slurry of the pigment is reduced in viscosity, the low-viscosity slurry is dispersed and stabilized for a long time, and the viscosity of the slurry under high shear is reduced. From the viewpoint of keeping it small, it is 25000 to 60000, preferably 35000 to 50000, and more preferably 40000 to 50000.

尚、ここで重量平均分子量(Mw)は、実施例に記載された測定法により測定された値である。   Here, the weight average molecular weight (Mw) is a value measured by the measuring method described in Examples.

また本発明の(A)成分、(B)成分それぞれの数平均分子量(Mn)は、顔料の高濃度スラリーを低粘度化し、低粘度化スラリーを長期分散安定化し、高剪断下におけるスラリーの粘度を小さく維持する観点から、20000〜40000であることが好ましく、25000〜38000が更に好ましく、27000〜35000が特に好ましい。また、(A)成分(B)成分それぞれのMw/Mnは3以下が好ましく、1.25〜3が更に好ましく、1.25〜2.5が特に好ましい。   In addition, the number average molecular weight (Mn) of each of the component (A) and the component (B) of the present invention is such that the high-concentration slurry of the pigment has a low viscosity, the low-viscosity slurry is long-term dispersed and stabilized, and the viscosity of the slurry under high shear is high. Is preferably 20000 to 40000, more preferably 25000 to 38000, and particularly preferably 27000 to 35000. Further, the Mw / Mn of each of the component (A) and the component (B) is preferably 3 or less, more preferably 1.25 to 3, and particularly preferably 1.25 to 2.5.

本発明の分散剤は、シェアの影響によるスラリー粘度の変化が小さくなり、塗布方法の適応性(スプレーやハケのいずれの塗布方法でも対応可能)に優れる観点から、(A)成分及び(B)成分を、(A)/(B)=50/50〜96/4(重量比)の割合で含有するが、55/45〜85/15が好ましく、60/40〜80/20が更に好ましい。   In the dispersant of the present invention, the change in the slurry viscosity due to the influence of the share becomes small, and from the viewpoint of excellent adaptability of the coating method (which can be applied by any spraying or brushing coating method), the component (A) and the component (B) Although a component is contained in the ratio of (A) / (B) = 50 / 50-96 / 4 (weight ratio), 55 / 45-85 / 15 are preferable and 60 / 40-80 / 20 are still more preferable.

本発明の分散剤は、顔料の高濃度スラリーを低粘度化し、低粘度化スラリーを長期分散安定化し、高剪断下におけるスラリーの粘度を小さく維持する観点から、カルシウムイオン80mg/L存在下でのクレー分散能は15%以上50%未満が好ましく、20〜45%が更に好ましい。また、マグネシウムイオン21mg/L存在下でのクレー分散能は46%以上60%未満が好ましく、46〜59%が更に好ましい。カルシウムイオン捕捉能は270mgCaCO3/g以上380mgCaCO3/g未満が好ましく、290〜379mgCaCO3/gが更に好ましい。 The dispersant of the present invention has a low viscosity of a high-concentration slurry of pigment, stabilizes the low-viscosity slurry for a long period of time, and maintains a low viscosity of the slurry under high shear, in the presence of 80 mg / L of calcium ions. The clay dispersibility is preferably 15% or more and less than 50%, more preferably 20 to 45%. The clay dispersibility in the presence of 21 mg / L of magnesium ions is preferably 46% or more and less than 60%, and more preferably 46 to 59%. Calcium ion capturing ability is preferably less than 270mgCaCO 3 / g or more 380mgCaCO 3 / g, more preferably 290~379mgCaCO 3 / g.

尚、本発明でいう「クレー分散能」及び「カルシウムイオン捕捉能」は、実施例に記載された測定法により測定されるものであり、無機顔料用分散剤の特性の指標として用いられる値である。   The “clay dispersibility” and “calcium ion scavenging ability” as used in the present invention are measured by the measurement methods described in the examples, and are values used as indicators of the properties of the dispersant for inorganic pigments. is there.

本発明の分散剤中の(A)成分と(B)成分の合計含有量は、顔料の高濃度スラリーを低粘度化できる範疇において、90〜100重量%が好ましく、95〜100重量%が更に好ましい。本発明の分散剤は、(A)成分及び(B)成分以外に未反応の不飽和一塩基酸、不飽和二塩基酸等を含有していてもよい。   The total content of the component (A) and the component (B) in the dispersant of the present invention is preferably 90 to 100% by weight, more preferably 95 to 100% by weight, in the category where the viscosity of the high concentration slurry of the pigment can be reduced. preferable. The dispersant of the present invention may contain unreacted unsaturated monobasic acid, unsaturated dibasic acid and the like in addition to the components (A) and (B).

本発明の(A)成分及び(B)成分の製造法は特に限定されないが、例えば以下に示す方法で製造することができる。   Although the manufacturing method of (A) component and (B) component of this invention is not specifically limited, For example, it can manufacture by the method shown below.

不飽和二塩基酸及びイオン交換水を不飽和二塩基酸の濃度が37重量%以上となるように反応容器に仕込み、75℃に加熱後、NaOH水溶液を不飽和二塩基酸の仕込量の2倍のモル数で仕込み、不飽和二塩基酸のNa塩とする。次に約100℃まで加熱した後、この温度で不飽和一塩基酸水溶液を、不飽和一塩基酸/不飽和二塩基酸(モル比)が、上記範囲となるように、また過酸化水素水溶液を過酸化水素が不飽和一塩基酸と不飽和二塩基酸の全仕込みモル数に対して17〜50モル%となるように、それぞれを3〜5時間かけて滴下し重合反応を行う。滴下終了後、100℃で1〜10時間熟成する。反応終了後、約60℃に冷却し、pHが8〜9となるようにアルカリ水溶液を仕込み、不飽和一塩基酸−不飽和二塩基酸共重合体のNa塩とする。   An unsaturated dibasic acid and ion-exchanged water are charged into a reaction vessel so that the concentration of the unsaturated dibasic acid is 37% by weight or more, heated to 75 ° C., and then an aqueous NaOH solution is added to the amount of the unsaturated dibasic acid charged to 2. Charge in double moles to make Na salt of unsaturated dibasic acid. Next, after heating to about 100 ° C., the unsaturated monobasic acid aqueous solution is heated at this temperature so that the unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) falls within the above range. Are added dropwise over 3 to 5 hours so that hydrogen peroxide is 17 to 50 mol% with respect to the total number of moles of unsaturated monobasic acid and unsaturated dibasic acid charged, and a polymerization reaction is carried out. After completion of dropping, the mixture is aged at 100 ° C. for 1 to 10 hours. After completion of the reaction, the reaction solution is cooled to about 60 ° C., and an alkaline aqueous solution is added so that the pH is 8 to 9, thereby obtaining an Na salt of an unsaturated monobasic acid-unsaturated dibasic acid copolymer.

本発明において対象となる無機顔料は、炭酸カルシウム、リン酸カルシウム、リン酸亜鉛、クレー、ベントナイト、サチンホワイト、亜鉛華、ベンガラ、フェライト、酸化チタン、アルミナ、酸化マグネシウム、タルク、ホワイトカーボン、セメント、石膏、カーボンブラック、チタン酸塩、珪酸塩等が挙げられ、炭酸カルシウムや、チタン酸バリウム等のチタン酸塩が好ましい。   Inorganic pigments of interest in the present invention are calcium carbonate, calcium phosphate, zinc phosphate, clay, bentonite, satin white, zinc white, bengara, ferrite, titanium oxide, alumina, magnesium oxide, talc, white carbon, cement, gypsum, Examples thereof include carbon black, titanate, and silicate, and calcium carbonate and titanate such as barium titanate are preferable.

具体的には、本発明の分散剤は、軽質炭酸カルシウム製造工程用、炭酸カルシウム湿式粉砕用、紙コーティング塗料用、フェライト製造工程用又はチタン酸バリウム等の電子材料用の分散剤として有効である。また、アルミナ等のセラミック用顔料に対しても有効である。   Specifically, the dispersant of the present invention is effective as a dispersant for light calcium carbonate production process, calcium carbonate wet grinding, paper coating paint, ferrite production process or electronic materials such as barium titanate. . It is also effective for ceramic pigments such as alumina.

本発明の分散剤は、塗工紙用、電子材料用又はセラミック用等の顔料分散組成物を得る際に有効に用いることができ、特に塗工紙用として用いることが好ましい。顔料分散組成物は、本発明の分散剤を用いて無機顔料の粉体、粉体の原鉱石又は粗粒子等を水系媒体中に分散させることにより得ることができる。水系媒体としては水、あるいは水と、エチルアルコール、エチレングリコール等の水溶性有機溶媒との混合溶液が挙げられ、好ましくは水である。   The dispersant of the present invention can be used effectively when obtaining a pigment dispersion composition for coated paper, electronic materials, ceramics, etc., and is particularly preferably used for coated paper. The pigment dispersion composition can be obtained by dispersing an inorganic pigment powder, powder ore or coarse particles in an aqueous medium using the dispersant of the present invention. Examples of the aqueous medium include water or a mixed solution of water and a water-soluble organic solvent such as ethyl alcohol or ethylene glycol, preferably water.

顔料分散組成物中の顔料の含有量は、特に規定されないが、乾燥効率を向上し、生産性を高める観点から、50重量%以上が好ましく、50〜85重量%がより好ましく、65〜85重量%が特に好ましい。また、顔料分散組成物中の本発明の分散剤の含有量は特に規定されないが、無機顔料100重量部に対して通常0.01〜10重量部が好ましく、0.05〜6重量部がさらに好ましく、0.05〜5重量部が特に好ましい。   The content of the pigment in the pigment dispersion composition is not particularly defined, but is preferably 50% by weight or more, more preferably 50 to 85% by weight, and more preferably 65 to 85% from the viewpoint of improving the drying efficiency and increasing the productivity. % Is particularly preferred. Further, the content of the dispersant of the present invention in the pigment dispersion composition is not particularly defined, but is usually preferably 0.01 to 10 parts by weight, more preferably 0.05 to 6 parts by weight with respect to 100 parts by weight of the inorganic pigment. 0.05 to 5 parts by weight is preferable.

本発明の分散剤を使用して、顔料分散組成物を得る方法としては、通常のスラリー化方法が用いられる。例えば分散剤を溶解した水溶液に顔料を添加して撹拌、混合する方法、顔料に水と分散剤を加えて撹拌、混合する方法等が挙げられる。撹拌、混合する方法としては、例えば高速ディスパー、ホモミキサー、ボールミル等一般に用いられる撹拌装置を使用することができる。   As a method for obtaining a pigment dispersion composition using the dispersant of the present invention, a usual slurrying method is used. For example, a method of adding a pigment to an aqueous solution in which a dispersant is dissolved and stirring and mixing, a method of adding water and a dispersant to the pigment, stirring and mixing, and the like can be mentioned. As a method of stirring and mixing, for example, a generally used stirring device such as a high-speed disper, a homomixer, or a ball mill can be used.

また、顔料の鉱石又は粗粒子を粉砕と同時にスラリー化する場合には、顔料の鉱石又は粗粒子に水と分散剤を添加して、粉砕と同時にスラリー化する方法等が挙げられる。粉砕と同時にスラリー化する方法としてはビーズミル等一般に用いられる湿式粉砕機を使用することが出来る。   In addition, when slurrying the pigment ore or coarse particles at the same time as pulverization, a method of adding water and a dispersant to the pigment ore or coarse particles and slurrying at the same time as the pulverization may be mentioned. A generally used wet pulverizer such as a bead mill can be used as a method of slurrying simultaneously with pulverization.

本発明において、シェアの影響によるスラリー粘度の変化を検討する方法としてTI値(チキソトロピック・インデックス)がある。これは調製したスラリーを一定の温度でB型粘度計にてスラリー粘度を測定するが、その際粘度計のローター回転速度を6rpmと60rpmでそれぞれ測定し、以下の式で算出するものである。   In the present invention, there is a TI value (thixotropic index) as a method for examining the change in slurry viscosity due to the influence of shear. In this method, the slurry viscosity of the prepared slurry is measured with a B-type viscometer at a constant temperature. At that time, the rotor rotational speed of the viscometer is measured at 6 rpm and 60 rpm, respectively, and the following formula is calculated.

TI値=(6rpmで測定時の粘度)/(60rpmで測定時の粘度)
60rpmで測定時の粘度の方がシェアがかかる状態であり、TI値が小さい程シェアの影響によるスラリー粘度の変化が少なくなる。TI値は3以下が好ましく、1〜2.5が更に好ましい。
TI value = (viscosity when measured at 6 rpm) / (viscosity when measured at 60 rpm)
The viscosity at the time of measurement at 60 rpm is a state in which the shear is applied, and the smaller the TI value, the smaller the change in slurry viscosity due to the influence of the shear. The TI value is preferably 3 or less, more preferably 1 to 2.5.

本発明の顔料分散組成物においては、TI値が小さい、即ちスラリー粘度の変化が小さい。このような格別顕著に優れた効果を発現する理由は定かではないが、シェアの影響を受けることなくスラリー粘度の変化が小さいという観点においては、おそらく無機顔料に対し、(A)成分は表面電位の付与による静電斥力の向上に、(B)成分は吸着力の向上にそれぞれ寄与していることに基づくものと考えられる。   In the pigment dispersion composition of the present invention, the TI value is small, that is, the change in slurry viscosity is small. The reason why such a remarkably excellent effect is manifested is not clear, but from the viewpoint that the change in slurry viscosity is small without being affected by the share, the component (A) is probably the surface potential for inorganic pigments. It is considered that the component (B) contributes to the improvement of the attractive force due to the improvement of the electrostatic repulsion by the application of.

以下の例において、無機顔料用分散剤の物性は以下の方法で測定した。   In the following examples, the physical properties of the dispersant for inorganic pigment were measured by the following methods.

<重量平均分子量>
GPC(ゲルパーミエーションクロマトグラフィー)により、下記条件で測定した。
カラム:TSK PWXL+G4000PWXL+G2500PWXL(いずれも東ソー株式会社製)
カラム温度:40℃
検出器:RI又はUV(210nm)
溶離液:0.2mol/L リン酸緩衝液/アセトニトリル(9/1)
流速:1.0mL/min
注入量:0.1mL
標準:ポリエチレングリコール
<クレー分散能>
下記の手順で行った。尚、塩化カルシウム・2水和物を用いた方法がカルシウムイオン80mg/L存在下でのクレー分散能を、また塩化マグネシウム・6水和物を用いた方法がマグネシウムイオン21mg/L存在下でのクレー分散能を示す。
1) グリシン67.56g、塩化ナトリウム52.6g及び1N−NaOH水溶液60mLにイオン交換水を加えて600gとしたグリシン緩衝液を調製する。
2) 塩化カルシウム・2水和物0.3268g又は塩化マグネシウム・6水和物0.1937gと、1)の調製液60gにイオン交換水を加えて1000gとし、分散液を調製する。
3) 0.1重量%(固形分換算)無機顔料用分散剤水溶液を20g調製する。
4) 試験管にJIS試験用粉体1,8種(関東ローム,微粒:日本粉体工業技術協会)のクレー0.3gを入れ、2)の調製液27gと3)の調製液3gを添加する。
5) 試験管をパラフィルムで密封した後、試験管を振り、試験管の底に塊がなくなったのを確認してから、試験管を上下に20回振る。
6) 5)の試験管を直射日光のあたらない所に20時間静置する。
7) 20時間後、分散液の上澄み5mLをホールピペットで20mLのスクリュー管に採取する。
8) UV分光器で透過率(T%)を測定する(波長380nm、1cmセル)。
100からT%の値を差し引いた値をクレー分散能(濁度)とする。
<Weight average molecular weight>
It measured by GPC (gel permeation chromatography) on the following conditions.
Column: TSK PWXL + G4000PWXL + G2500PWXL (both manufactured by Tosoh Corporation)
Column temperature: 40 ° C
Detector: RI or UV (210 nm)
Eluent: 0.2 mol / L phosphate buffer / acetonitrile (9/1)
Flow rate: 1.0 mL / min
Injection volume: 0.1 mL
Standard: Polyethylene glycol <Clay dispersibility>
The following procedure was followed. It should be noted that the method using calcium chloride dihydrate has the ability to disperse clay in the presence of 80 mg / L calcium ion, and the method using magnesium chloride hexahydrate has the ability to use 21 mg / L magnesium ion. Shows clay dispersibility.
1) Prepare a glycine buffer solution by adding ion exchange water to 60.56 g of glycine, 52.6 g of sodium chloride and 60 mL of 1N NaOH aqueous solution to make 600 g.
2) Add ion-exchanged water to 1000 g of calcium chloride dihydrate 0.3268 g or magnesium chloride hexahydrate 0.1937 g and 60 g of the prepared solution of 1) to prepare a dispersion.
3) Prepare 20 g of 0.1 wt% (solid content conversion) inorganic pigment dispersant aqueous solution.
4) Put 0.3g of JIS test powder 1,8 types (Kanto loam, fine particles: Japan Powder Industrial Technology Association) into the test tube, and add 2g of preparation liquid 27g and 3g of preparation liquid 3g. To do.
5) After sealing the test tube with parafilm, shake the test tube and check that there is no lump at the bottom of the test tube, then shake the test tube up and down 20 times.
6) Leave the test tube of 5) in a place not exposed to direct sunlight for 20 hours.
7) After 20 hours, collect 5 mL of the supernatant of the dispersion with a whole pipette into a 20 mL screw tube.
8) Measure the transmittance (T%) with a UV spectrometer (wavelength 380 nm, 1 cm cell).
The value obtained by subtracting the value of T% from 100 is defined as clay dispersibility (turbidity).

<カルシウムイオン捕捉能>
1) カルシウムイオン標準水溶液を調製する。
<Calcium ion scavenging ability>
1) Prepare a standard calcium ion solution.

0.01mol/Lカルシウムイオン水溶液:塩化カルシウム二水和物1.4701gをイオン交換水1kgに溶解したもの
0.001mol/Lカルシウムイオン水溶液:上記0.01mol/Lカルシウムイオン水溶液100gにイオン交換水を加えて1kgにしたもの
0.0001mol/Lカルシウムイオン水溶液:上記0.001mol/Lカルシウムイオン水溶液10gにイオン交換水を加えて100gにしたもの
2) 100mLビーカーに無機顔料用分散剤を固形分換算で10mg及び0.001mol/Lのカルシウムイオン水溶液50gを加える。
3) 1)の各水溶液50gと2)の水溶液をマグネチックスターラーで撹拌する。
4) 3)の各水溶液にpHが9〜11になるように4.8重量%NaOH水溶液を加える。
5) 4)の各水溶液に、4M−KCl水溶液を1mL加える。
6) オリオン社製イオンアナライザーEA920を用いて、オリオン社製カルシウムイオン電極93−20によりカルシウムイオン量を測定する。
7) 検量線から無機顔料用分散剤により捕捉されたカルシウムイオン量を測定し、分散剤の固形分1g当たりの捕捉量を炭酸カルシウム換算のmg数で表し、その値をカルシウムイオン捕捉能とする。
0.01 mol / L calcium ion aqueous solution: a solution obtained by dissolving 1.4701 g of calcium chloride dihydrate in 1 kg of ion exchange water 0.001 mol / L calcium ion aqueous solution: ion exchange water to 100 g of the above 0.01 mol / L calcium ion aqueous solution Added to make 1 kg 0.0001 mol / L calcium ion aqueous solution: 100 g obtained by adding ion-exchanged water to 10 g of the above 0.001 mol / L calcium ion aqueous solution
2) Into a 100 mL beaker, add 10 mg of the inorganic pigment dispersant and 50 g of 0.001 mol / L calcium ion aqueous solution in terms of solid content.
3) Stir 50 g of each aqueous solution of 1) and the aqueous solution of 2) with a magnetic stirrer.
4) Add 4.8 wt% NaOH aqueous solution to each aqueous solution of 3) so that the pH is 9-11.
5) Add 1 mL of 4M-KCl aqueous solution to each aqueous solution of 4).
6) Using an Orion ion analyzer EA920, measure the amount of calcium ions with an Orion calcium ion electrode 93-20.
7) Measure the amount of calcium ions captured by the dispersant for inorganic pigment from the calibration curve, express the amount captured per gram of the solid content of the dispersant in mg in terms of calcium carbonate, and use that value as the calcium ion scavengeability. .

製造例1
攪拌機、温度計、還流冷却管、窒素導入管、滴下ロートを備えた反応容器に、マレイン酸無水物49.0g及びイオン交換水54.3gを仕込み、75℃に加熱後、30重量%NaOH水溶液133.3gを滴下し、マレイン酸Na塩水溶液とした。次に窒素気流下で100℃まで加熱した後、この温度を維持しながら、80重量%アクリル酸水溶液225.3g及び35重量%過酸化水素水溶液109.3gをそれぞれ別の滴下ロートから3時間かけて滴下し重合反応を行った。滴下終了後、100℃で7時間熟成し重合反応を完結させた。反応終了後、冷却し、約60℃を保持しながらpHが6〜8となるように30重量%NaOH水溶液で中和して、アクリル酸―マレイン酸共重合体のナトリウム塩を得た。これを共重合体A1という。
Production Example 1
A reaction vessel equipped with a stirrer, thermometer, reflux condenser, nitrogen inlet tube, and dropping funnel was charged with 49.0 g of maleic anhydride and 54.3 g of ion-exchanged water, heated to 75 ° C., and then a 30 wt% NaOH aqueous solution. 133.3g was dripped and it was set as the maleic-acid sodium salt aqueous solution. Next, after heating to 100 ° C. under a nitrogen stream, while maintaining this temperature, 225.3 g of 80 wt% acrylic acid aqueous solution and 109.3 g of 35 wt% aqueous hydrogen peroxide solution were respectively added from another dropping funnel over 3 hours. The solution was added dropwise to carry out a polymerization reaction. After completion of the dropping, the mixture was aged at 100 ° C. for 7 hours to complete the polymerization reaction. After completion of the reaction, the reaction mixture was cooled and neutralized with a 30 wt% NaOH aqueous solution so as to have a pH of 6 to 8 while maintaining about 60 ° C. to obtain a sodium salt of an acrylic acid-maleic acid copolymer. This is called copolymer A1.

製造例2
表1に示すモノマーを用い、製造例1と同様にして共重合体A2〜A13を得た。
Production Example 2
Using monomers shown in Table 1, copolymers A2 to A13 were obtained in the same manner as in Production Example 1.

製造例1〜2で得られた共重合体A1〜A13のモノマー組成、重量平均分子量(Mw)、数平均分子量(Mn)及びMw/Mnをまとめて表1に示す。尚、共重合体A1〜A8,A10,A11及びA13が本発明の(A)成分である。   Table 1 shows the monomer composition, weight average molecular weight (Mw), number average molecular weight (Mn), and Mw / Mn of the copolymers A1 to A13 obtained in Production Examples 1 and 2. The copolymers A1 to A8, A10, A11 and A13 are the component (A) of the present invention.

Figure 0004563065
Figure 0004563065

製造例3
攪拌機、温度計、還流冷却管、窒素導入管、滴下ロートを備えた反応容器に、マレイン酸無水物149.6g及びイオン交換水261.8gを仕込み、75℃に加熱後、30重量%NaOH水溶液231.4gを滴下し、マレイン酸Na塩水溶液とした。次に窒素気流下で100℃まで加熱した後、この温度を維持しながら、80重量%アクリル酸水溶液172.1g及び35重量%過酸化水素水溶液30.3gをそれぞれ別の滴下ロートから3時間かけて滴下し重合反応を行った。滴下終了後、100℃で7時間熟成し重合反応を完結させた。反応終了後、冷却し、約60℃を保持しながらpHが6〜8となるように30重量%NaOH水溶液で中和して、アクリル酸―マレイン酸共重合体のナトリウム塩を得た。これを共重合体B1という。
Production Example 3
A reaction vessel equipped with a stirrer, thermometer, reflux condenser, nitrogen inlet tube, and dropping funnel was charged with 149.6 g of maleic anhydride and 261.8 g of ion-exchanged water, heated to 75 ° C., and then 30% by weight NaOH aqueous solution. 231.4g was dripped and it was set as the maleic acid Na salt aqueous solution. Next, after heating to 100 ° C. under a nitrogen stream, while maintaining this temperature, 172.1 g of 80 wt% aqueous acrylic acid solution and 30.3 g of 35 wt% aqueous hydrogen peroxide solution were respectively added from another dropping funnel over 3 hours. The solution was added dropwise to carry out a polymerization reaction. After completion of the dropwise addition, the mixture was aged at 100 ° C. for 7 hours to complete the polymerization reaction. After completion of the reaction, the reaction mixture was cooled and neutralized with a 30 wt% NaOH aqueous solution so as to have a pH of 6 to 8 while maintaining about 60 ° C. to obtain a sodium salt of an acrylic acid-maleic acid copolymer. This is called copolymer B1.

製造例4
表2に示すモノマーを用い、製造例3と同様にして共重合体B2〜B13を得た。
Production Example 4
Using monomers shown in Table 2, copolymers B2 to B13 were obtained in the same manner as in Production Example 3.

製造例3〜4で得られた共重合体B1〜B13のモノマー組成、重量平均分子量(Mw)、数平均分子量(Mn)及びMw/Mnをまとめて表2に示す。尚、共重合体B1〜B9及びB13が本発明の(B)成分である。   Table 2 shows the monomer composition, weight average molecular weight (Mw), number average molecular weight (Mn), and Mw / Mn of the copolymers B1 to B13 obtained in Production Examples 3 to 4. The copolymers B1 to B9 and B13 are the component (B) of the present invention.

Figure 0004563065
Figure 0004563065

実施例1
製造例で得られた共重合体A1〜A13と共重合体B1〜B13とを、表3に示す割合で配合し、本発明の分散剤1〜8及び比較分散剤1〜6を得た。
Example 1
Copolymers A1 to A13 and Copolymers B1 to B13 obtained in Production Examples were blended in the ratios shown in Table 3 to obtain dispersants 1 to 8 and comparative dispersants 1 to 6 of the present invention.

得られた分散剤のカルシウムイオン又はマグネシウムイオン存在下でのクレー分散能、及びカルシウムイオン捕捉能をまとめて表3に示す。   Table 3 shows the clay dispersibility in the presence of calcium ions or magnesium ions and the calcium ion scavengeability of the obtained dispersant.

Figure 0004563065
Figure 0004563065

実施例2
ディスポビーカー300mLに平均粒径が0.4μmの酸化チタン148g、及びスラリー濃度が75重量%になるようにイオン交換水と、分散剤1〜8又は比較分散剤1〜6(酸化チタン100重量部に対して1重量部)を仕込んだ後、特殊機化工業株式会社製のホモディスパーで攪拌(2500rpm×2分間)し、スラリー(顔料分散組成物)を調製した。得られたスラリーを株式会社東京計器製のB型粘度装置を用いて25℃におけるB粘度をローターの回転速度6rpm、60rpmでそれぞれ1分後に測定した。また得られた粘度値からTI値を算出した。結果を表4に示す。実施例においては、ローターの回転速度6rpm及び60rpmで測定したときのスラリー粘度の値は共に低く、かつ、TI値が3以下であり、良好な顔料分散組成物が得られていることがわかる。
Example 2
Disposable beaker 300 mL, titanium oxide 148 g with an average particle size of 0.4 μm, and ion-exchanged water and dispersant 1-8 or comparative dispersant 1-6 (100 parts by weight of titanium oxide) so that the slurry concentration becomes 75% by weight. 1 part by weight) was added, and the mixture was stirred (2500 rpm × 2 minutes) with a homodisper manufactured by Tokushu Kika Kogyo Co., Ltd. to prepare a slurry (pigment dispersion composition). The obtained slurry was measured for B viscosity at 25 ° C. using a B-type viscometer manufactured by Tokyo Keiki Co., Ltd. at a rotor rotational speed of 6 rpm and 60 rpm after 1 minute. Further, the TI value was calculated from the obtained viscosity value. The results are shown in Table 4. In the examples, the values of the slurry viscosity when measured at a rotor rotational speed of 6 rpm and 60 rpm are both low, and the TI value is 3 or less, indicating that a good pigment dispersion composition is obtained.

Figure 0004563065
Figure 0004563065

Claims (5)

下記の(A)成分及び(B)成分を、(A)/(B)=50/50〜96/4(重量比)の割合で含有する無機顔料用分散剤であって、(A)成分及び(B)成分の数平均分子量(Mn)が、それぞれ20000〜40000であり、Mw/Mn≦3である無機顔料用分散剤
(A)成分:
構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=91/9〜74/26で、重量平均分子量(Mw)が25000〜60000である、不飽和一塩基酸と不飽和二塩基酸との共重合体の塩
(B)成分:
構成モノマー単位比率が、不飽和一塩基酸/不飽和二塩基酸(モル比)=63/37〜47/53で、重量平均分子量(Mw)が25000〜60000である、不飽和一塩基酸と不飽和二塩基酸との共重合体の塩
A dispersant for inorganic pigment containing the following component (A) and component (B) in a ratio of (A) / (B) = 50/50 to 96/4 (weight ratio), wherein component (A) And the number average molecular weight (Mn) of (B) component is 20000-40000, respectively, and the dispersing agent for inorganic pigments which is Mw / Mn <= 3 .
(A) component:
An unsaturated monobasic acid having a constituent monomer unit ratio of unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 91/9 to 74/26 and a weight average molecular weight (Mw) of 25,000 to 60,000 Salt (B) component of copolymer with unsaturated dibasic acid:
An unsaturated monobasic acid having a constituent monomer unit ratio of unsaturated monobasic acid / unsaturated dibasic acid (molar ratio) = 63/37 to 47/53 and a weight average molecular weight (Mw) of 25,000 to 60,000 Salts of copolymers with unsaturated dibasic acids
カルシウムイオン80mg/L存在下でのクレー分散能が15%以上50%未満、マグネシウムイオン21mg/L存在下でのクレー分散能が46%以上60%未満であり、カルシウムイオン捕捉能が270mgCaCO3/g以上380mgCaCO3/g未満である請求項1記載の無機顔料用分散剤。 The clay dispersibility in the presence of 80 mg / L of calcium ions is 15% or more and less than 50%, the clay dispersibility in the presence of 21 mg / L of magnesium ions is 46% or more and less than 60%, and the calcium ion scavenging ability is 270 mgCaCO 3 / g or more 380mgCaCO 3 / inorganic pigment dispersant of claim 1 Symbol placement than a is g. 不飽和一塩基酸がアクリル酸及びメタクリル酸から選ばれる少なくとも1種である請求項1又は2記載の無機顔料用分散剤。 The inorganic pigment dispersant according to claim 1 or 2, wherein the unsaturated monobasic acid is at least one selected from acrylic acid and methacrylic acid. 不飽和二塩基酸がマレイン酸無水物、マレイン酸及びイタコン酸から選ばれる少なくとも1種である請求項1〜いずれか記載の無機顔料用分散剤。 The dispersant for inorganic pigments according to any one of claims 1 to 3, wherein the unsaturated dibasic acid is at least one selected from maleic anhydride, maleic acid and itaconic acid. 請求項1〜いずれか記載の無機顔料用分散剤を含有する顔料分散組成物。



The pigment dispersion composition containing the dispersing agent for inorganic pigments in any one of Claims 1-4 .



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Publication number Priority date Publication date Assignee Title
JPS5957913A (en) * 1982-09-29 1984-04-03 Okutama Kogyo Kk Production of high concentration slurry of synthetic calcium carbonate having good fluidity
JPS59193964A (en) * 1983-04-15 1984-11-02 Sannopuko Kk Dispersing agent for light calcium carbonate
JPS60137429A (en) * 1983-12-26 1985-07-22 Lion Corp Dispersant for calcium carbonate
JPH08188986A (en) * 1995-01-05 1996-07-23 Lion Corp Pigment dispersant for coatd paper

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5957913A (en) * 1982-09-29 1984-04-03 Okutama Kogyo Kk Production of high concentration slurry of synthetic calcium carbonate having good fluidity
JPS59193964A (en) * 1983-04-15 1984-11-02 Sannopuko Kk Dispersing agent for light calcium carbonate
JPS60137429A (en) * 1983-12-26 1985-07-22 Lion Corp Dispersant for calcium carbonate
JPH08188986A (en) * 1995-01-05 1996-07-23 Lion Corp Pigment dispersant for coatd paper

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