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JP4614023B2 - Pigment dispersing apparatus and pigment dispersing method - Google Patents

Pigment dispersing apparatus and pigment dispersing method Download PDF

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Publication number
JP4614023B2
JP4614023B2 JP16665699A JP16665699A JP4614023B2 JP 4614023 B2 JP4614023 B2 JP 4614023B2 JP 16665699 A JP16665699 A JP 16665699A JP 16665699 A JP16665699 A JP 16665699A JP 4614023 B2 JP4614023 B2 JP 4614023B2
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Prior art keywords
pigment
liquid medium
dispersion
resin
water
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JP16665699A
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JP2000351916A (en
Inventor
勲 田林
治 尾島
律子 土井
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DIC Corp
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DIC Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/53Mixing liquids with solids using driven stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/56Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/2805Mixing plastics, polymer material ingredients, monomers or oligomers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/35Mixing inks or toners
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/116Stirrers shaped as cylinders, balls or rollers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/70Mixers specially adapted for working at sub- or super-atmospheric pressure, e.g. combined with de-foaming
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0032Pigments, colouring agents or opacifiyng agents

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Ink Jet Recording Methods And Recording Media Thereof (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は,減圧しながら分散可能な顔料分散装置及び顔料分散方法及び着色樹脂粒子分散液製造方法に関する。より詳しくは,インクジェット記録用顔料インクの顔料および着色樹脂粒子分散液の分散装置及び製造方法に関する。
【0002】
【従来の技術】
インクジェット記録用インクは大別すると油性インクと水性インクがあるが,油性インクは臭気・毒性の点で問題があり,水性インクが主流となりつつある。
【0003】
しかしながら,従来の水性インクの多くは着色剤として水溶性染料を用いているため耐水性や耐光性が悪いという欠点を有していた。また,染料が分子レベルで溶解しているため,オフィスで一般に使用されているコピー用紙などのいわゆる普通紙に印刷すると髭状のフェザリングと呼ばれるブリードを生じて著しい印刷品質の低下を招いていた。
【0004】
上記欠点を改良するためにいわゆる水性の顔料インクが過去に様々に提案されており,例えばバインダー兼分散剤として水溶性樹脂を用いてカ−ボンブラックや有機顔料を分散させた樹脂溶解型のインクやポリマーラテックスあるいはマイクロカプセルとして着色剤を内包する樹脂分散型のインクが各種提案されている。
【0005】
ジェットプリンター用水性顔料インクとしては,なるべく微粒子径に分散された着色剤粒子が求められており,具体的な樹脂溶解型の水性インクの例として,特許第2512861号公報では,(a)顔料とポリマー分散剤とを2−ロールミリング装置に充填し;(b)摩砕して顔料とポリマー分散剤との分散体を得;そして(c)この顔料分散体を水性キャリア媒体中に分散させる工程からなる,改良された特性を有する水性の顔料入りインクジェット用インクの調整方法が,特開平3−153775号公報では,a)顔料とカルボキシル基含有ポリアクリル系樹脂とを含有する固体顔料調合物b)水で希釈可能な有機溶媒c)湿潤剤d)水を含有するインクジェット印刷用水性インク組成物が提案されている。
【0006】
樹脂分散型の水性インクは,インクの水分蒸発に伴う粘度上昇は比較的少なく,また耐水性に優れるという利点がある。具体的には,特開昭58−45272号公報では染料を含有したウレタンポリマーラテックスを含むインク組成物,特開昭62−95366号公報では水不溶性有機溶媒中にポリマーと油性染料を溶解し,さらに表面活性剤を含む水溶液と混合して乳化させた後に溶媒を蒸発してポリマー粒子中に内包された染料を含むインクが提案され,特開昭62−254833号公報ではカプセル化時の有機溶媒と水との間の界面張力を10ダイン以下にすることによる着色料水性懸濁液の製造法が提案され,特開平1−170672号公報では同様にマクロカプセル化した色素を含有する記録液等が提案されている。
【0007】
しかしながら,これらの技術は顔料の微粒子化には有効なものの,分散している着色剤の分散安定性やノズルからの噴射安定性が必ずしも十分ではなく,印刷品質も必ずしも良くはなかった。
【0008】
インクの吐出安定性を向上させる手段として,減圧(真空)下及び/又は超音波処理する方法が知られており,具体的には特開平06−184479号公報の記録液では,水性媒体と特定アゾ色素の少なくとも1種とを充分に混合して溶解し,孔径1μのテフロンフイルタ−で加圧濾過した後,真空ポンプ及び超音波洗浄器で脱気処理する方法,特開平06− 25574号公報のインキジエツトプリンタ−用インキでは連続液相,不連続相及び固相からなる微細分散三相懸濁液を含むインキ,具体的には,例えば,カ−ボンブラツク等の顔料からなる固相をオレイン酸に分散させた微細分散液と乳化補助剤であるソルビタンモノステアレ−トとを含む疎水相に,乳化剤であるトリエタノ−ルアミン,乳化補助剤及び水を含む親水性相を撹拌下に添加した後,得られた懸濁液を超音波処理することにより,前記の三相懸濁液を得る方法,特開平09−286943号公報の記録液の処理方法では,少なくとも分散剤,水性液媒体,顔料,水から構成される水性顔料系記録液を,調製,精製した後,超音波処理 ,並びに真空脱泡処理を行う方法が開示されている。
【0009】
しかしながら,これらの技術は超音波そのものは顔料分散効果を有しておらず,顔料の微粒子化や濡れ改良効果,及び脱泡効果が小さいために,顔料の分散安定性やノズルからの噴射安定性が必ずしも十分ではなく,印刷品質も必ずしも良くはなかった。
【0010】
一方,一般的な顔料分散方法としては特開昭61−163970号公報の塗料用着色材およびその製造法として,塗料用樹脂を含む溶液で顔料を湿潤処理し,溶液中に顔料を分散させた後,乾燥固化させ,顔料表面を塗料用樹脂で被覆することにより,塗膜の光学的性質等に優れた塗料用着色材を得る方法が,特開昭62−192471号公報の粉体塗料の製造方法では湿式分散機により溶剤に溶解された樹脂液中に顔料が均一に分散された分散物を,瞬間真空乾燥することにより,顔料分散性が格段に改善され,隠ぺい性,平滑性に優れた粉体塗料を得る方法が提案されており,インクジェット記録用インクの製造方法として応用が可能であるが,一度分散液を固化するため,再分散工程が必要であることに加えて,顔料の分散媒への濡れが不十分でインクの吐出安定性が不十分であった。
【0011】
また,特開平09−12933号公報の磁性塗料の製造方法では,連続式2軸混練機を用いて磁性塗料を混練する混練工程において,混練機の混練部を真空雰囲気下にして混練を行う方法が開示されているが,本製造方法の装置構成では磁性粉と塗料樹脂の溶融混練であり,湿式混練が不可能であった。
【0012】
また,一般に,減圧で顔料分散を行うことは知られているが,連続して効率よく顔料分散を行うことが可能な顔料分散装置は知られていなかった。
【0013】
【発明が解決しようとする課題】
本発明が解決しようとする課題は,微粒子径で分散安定性に優れ,かつインクジェット記録において安定した噴射と優れた印刷品質を可能にする,顔料を着色剤とするインク組成物を可能にする顔料分散装置及び顔料分散方法及び着色樹脂粒子製造方法を提供することにある。
【0014】
【課題を解決するための手段】
本発明者等は,上記の課題を解決するために鋭意研究を重ねた結果,本発明を解決するに至った。即ち本発明は,次の発明を提供する。
【0015】
(1)顔料分散装置
少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含み,固体顔料が液媒体に安定分散するまで,当該容器と分散機構との間に,当該混合物を連続的に循環させる機構を設けたことを特徴とするメジアミルからなる顔料分散装置。
【0016】
(2)顔料分散方法
少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含む顔料分散装置を用いて,固体顔料を液媒体に安定分散させるに当たり,当該混合物を循環させて,減圧下で,固体顔料を液媒体に安定分散させることを特徴とする顔料分散方法。
【0017】
以下,順に本発明を説明する。
【0018】
本発明の顔料分散装置は,少なくとも分散が行われる部分が減圧構造を有し,かつ分散液が連続的に通過するメジアミルである顔料分散装置で,好ましくは,分散液の供給及び/又は回収タンクから減圧を行うようにした顔料分散装置である。
【0019】
本発明の顔料分散装置は,少なくとも次の構成を有する。
▲1▼液媒体(分散媒に対応する)と,固体顔料との混合物を入れる,減圧可能な構造を有する容器を有する。
▲2▼運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルを有する。
▲3▼固体顔料を液媒体に安定分散するまで,前記▲1▼の容器と分散機構との間に,前記▲1▼の混合物を連続的に循環させる機構を有する。
【0020】
本発明の顔料分散装置の最大の特徴は,上記▲1▼と▲3▼とを兼備する点にある。
【0021】
本発明の好ましい分散装置であるメジアミルとしては,公知慣用のビーズミルやボールミルがいずれも使用できるが,例えば,分散技術入門(日刊工業新聞社;小石真純,釣谷泰一著)による分類の,通過型ミル(サンドミル,連続式アトライター,パールミル,モリネックス)及びそれらの変形ミル(ドライスヴェルケ製DCPミル,三井鉱山製SCミル,井上製作所製スパイクミル,シンマルエンタープライゼス製ダイノーミルECM,浅田鉄工製ナノミル等)が挙げられる。
【0022】
これらは分散メジア(ボールあるいはビーズ)の磨砕剪断力を利用して顔料の磨砕・分散を行う分散装置であるが,本発明では,減圧下でそれが行えるようにして用いる。
【0023】
中でも,固体顔料と液媒体との混合物が通過する,運動するメジア群を含む前記分散機構が,ベッセルの内壁に微小間隙を介して,外壁を有する回転可能なロータを有し,その微小間隙にメジアが運動可能となる様に充填されており,ロータを回転させるとともに,固体顔料と液媒体との混合物を,分散機構中で略栓流となる様にして通過させる様になっている環状メジアミルが,特に好ましい。
【0024】
固体顔料と液媒体との混合物を安定な固体顔料分散液とするに当たり,当該混合物を略栓流とするためには,上記に加えて,例えば,ロータ表面に,メジアに回転と衝撃力を与える突起と,当該混合物の流れ方向とは逆方向にメジアが戻される様に溝を形成する様にするのが好ましい。
【0025】
固体顔料と液媒体との混合物や,固体顔料分散液を冷却可能なように,少なくとも装置の一部に冷却構造を設けることが好ましい。具体的には,固体顔料と液媒体との混合物や,固体顔料分散液と直接接しないように,ロータ内部やベッセル外壁等に,冷却ジャケットを設けて,冷却水等の冷媒を通過させて,分散時の温度を調節する様にするのが好ましい。以下,この様な特に好ましいメジアミルをスパイクミルと称する。
【0026】
メジアミルのロータとベッセルとの微小間隙には分散のためのメジアが充填されている。本発明の分散に用いる分散メジアは,既存のものが使用可能であり,メジア径が細かいほど,密度が大きいほど,回転数が高いほど顔料の粉砕能力はアップする。分散メジアはガラスビーズやセラミックスビーズ,スチールボール,ステンレスボール,架橋樹脂ビーズなどが好ましく,顔料を微粒子にするには,なるべく細かい径のビーズが好ましい。そして,これらのメジアはメジアミルから外部には流出しない様になっている。
【0027】
本発明では,固体顔料と液媒体との混合物を入れる,減圧可能な構造を有する容器を有するが,固体顔料と液媒体との混合物を供給する供給容器,及び/又は,固体顔料が液媒体に安定分散した顔料分散液を回収する回収容器を有し,すくなくともいずれか一方から減圧を行う様にする。
【0028】
即ち,本発明では,供給容器と回収容器とを同一として,兼用容器として一つのみ用いる場合と,供給容器と回収容器とを別々に両方用いる場合とがある。前者の場合には,この一つの兼用容器から減圧を行い,後者の場合には,供給容器の圧力に対して,回収容器の圧力が負圧になる様に減圧を行うのが,好ましい。
【0029】
尚,容器に一部に超音波発信機構を設ける様にするのが,同一メジアミルを同一運転条件する場合には,より短時間で,安定な分散液が得られる点で好ましい。
【0030】
固体顔料を液媒体に安定分散するまで,前記各容器と分散機構との間に,固体顔料と液媒体との混合物を連続的に循環させる機構を設ける。この機構は,具体的には,管を設けてこれらを連結することにより,設けることが出来る。勿論,この配管部分にジャケットを設けて上記と同様に分散時の温度を調節する様にすることも出来,実際にも,そうすることが好ましい。
【0031】
メジアミルの分散が行われる部分を減圧とするには,例えば脱気をすれば良い。上記容器と管とを連結配管するならば,例えば,固体顔料と液媒体との混合物を入れておく,減圧可能な構造を有する容器の上方から減圧を行う様にすれば良い。
【0032】
本発明の顔料分散方法を実施するに当たっての分散温度や圧力は,特に制限されるものではなく,適宜選択すれば良いが,分散温度としては,循環系を全体を1〜20℃,好ましくは1〜10℃とし,循環系の圧力は,1〜500mmHg,好ましくは1〜100mmHgとする。インクジェット記録用水性インク用顔料分散液を得る場合には,印刷濃度がより高く安定である,長期連続印字における吐出安定性がより優れる等の点で,分散が行われる循環系は,温度1〜10℃で1〜100mmHgとするのが特に好ましい。
【0033】
こうした顔料分散装置を用いて前記混合物を,安定な固体顔料分散液となるまで,繰り返し循環させて,固体顔料の液媒体への分散を行う。安定な分散液を得るに当たっては,予め種種の条件にて循環の途中にて適宜サンプリングを行い,必要な安定性が保たれる様な条件を見い出してから,その最適条件にて実施することが好ましい。一般的には,分散安定性が一定となり飽和するまで処理作業を行う様にするのが好ましい。
【0034】
次に本発明の顔料分散装置を図面を用いて説明する。図1は,本発明の供給タンクと回収タンクが同一である,減圧構造を有する顔料分散装置1Aを示す。黒抜き矢印は,固体顔料の液媒体との混合物の流れ方向を,白抜き矢印は,装置を一定温度に保つための液媒体を通過させる,ジャケット(後述)内での流れ方向を示す(以下,同様。)。
【0035】
この装置は,脱気要素に相当する脱気用ポンプ(図示せず)と,減圧するの必要な脱気口6を設けた供給容器兼回収容器である,減圧可能な構造を有する容器に相当するタンク4と,メジアミルと,固体顔料の液媒体との混合物を連続的に循環させる機構である,タンク4とメジアミルとを連結する管7とからなっている。実使用時には,脱気用ポンプと脱気口6とを管で連結して,系を減圧状態とする。
【0036】
このタンク4の内部の側部には,超音波発信機構に相当する超音波発振器5が設けられており,一方,タンク4と,固体顔料の液媒体との混合物を供給する側の管4の外部に,ジャケットを設けて,循環系が一定の温度に保てる様な仕組みとなっている。このタンク4の下部は管7により,メジアミルの入口(導入口)に連結されている。逆に,メジアミルの出口(排出口)は,タンク4に戻される様に管7により連結されており,これにより循環を行う。
【0037】
メジアミルの入口に対して,固体顔料と液媒体との混合物をより安定的に供給する際には,図示していないが,供給ポンプを設ける様にしても良い。
【0038】
メジアミルは,ベッセルと,ロータ3とを含み,ベッセルの壁2と,ロータ3の外壁との間に微小間隙を有しており,この間隙に,上記分散メジアが充填されている。このロータは環状であり,軸中心に回転する様になっており,固体顔料の液媒体との混合物を,管7を通してメジアミルの入口から導入し,この間隙に通過させると,ロータ3の回転によりメジア群が運動し,その剪断力により,固体顔料の液媒体への分散が起こり,入口よりは,より安定な分散状態となり,メジアミルの出口(排出口)より,管7へ排出される様になっている。メジアの回転や衝撃力に基づく運動量を大きくし,結果的に前記混合物に大きな剪断力が作用する様に,ロータ3の表面には凹凸が設けられている。
【0039】
ベッセルの外部にも同様に,ジャケットが設けられ,微小間隙の通過時においても,系内温度が一定の温度に保てる様な仕組みとなっている。
【0040】
こうすることにより,前記混合物や分散安定性が未だ不十分な分散液を減圧しながら循環分散が可能となる。
【0041】
図2は,本発明の供給容器と回収容器とを別々に両方有する,減圧構造を有する顔料分散装置1Bを示す。この装置1Bは,供給容器に対応する供給タンク4Aと,回収容器に対応する回収タンク4Bを有しており,各タンクには,装置1Aと同様に,脱気口6と超音波発振器5がそれぞれ設けられている。また,タンク4Aとメジアミルとを連結する管7の一部分に圧力調節弁8を,タンク4Aと4Bを連結する管7の一部分に切替弁9を設けてある。
【0042】
この装置1Bの場合には,供給タンク4Aの圧力に対して,回収タンク4Bの圧力が負圧となる様にして,即ち,タンク4Aよりも4Bの方がより高い減圧度となる様にして,固体顔料の液媒体への分散を行うのが,好ましい。
【0043】
具体的に,供給タンク4Aと回収タンク4Bを上記した様に個別に設置する場合には,供給タンク4A側を常圧か減圧に設定し,さらに供給タンク4Aの圧力に対して,回収タンク4Bの圧力を負圧になるようにする事により,メジアミル中の分散部分で減圧分散可能となる。この際の圧力調節に弁8,9を利用する。
【0044】
この時,固体顔料と液媒体との混合物をメジアミルの入口に供給するための供給ポンプを設けた場合にはそれの負荷を大幅に小さくすることが可能になり,場合によっては供給ポンプが不要となる。供給タンク4Aに受けた固体顔料と液媒体の混合物は,一度常圧に戻してから回収タンクに戻して,固体顔料の液媒体への分散安定性が飽和するまで,循環させて再度繰り返し分散を行うことが可能であるが,回収タンク4Bの減圧度以上の吸引ポンプで供給タンクに分散液を戻すことによって,常圧に戻すことなく分散を継続することが可能になる。
【0045】
この時,メジアミルは,分散部分の供給側に圧損を発生させる弁構造を設けたり,分散部分の断面積が小さく分散部分に大きな圧損が生じる様にした上記変形ミルを用いることが好ましい。
【0046】
図2の装置の場合,タンク4Aに充填された固体顔料と液媒体との混合物は,タンク4Aとタンク4Bとの圧力差によって,メジアミルのベッセル内に供給されるが,圧力調節弁8を絞ることによりベッセル内での負圧をコントロールすることができる。この時,タンク4Aとタンク4Bとの間の切替弁9は閉じられている。
【0047】
当該混合物の分散液がタンク4Bに回収された時点で,圧力調節弁8が閉じられ,タンク4Aと4Bの減圧度を逆転して切替弁8を開放にすると,該混合物はタンク4Aから4Bへ移動する。固体顔料と液媒体の混合物について,同様の操作を繰り返すことにより,繰り返しパス分散が可能となる。分散安定性が飽和して安定な分散液となるまでは,この繰り返しで,当該混合物の分散安定性は,より向上する。
【0048】
尚,当該混合物のメジアミル中での流量あるいは処理量は,循環分散の場合には,供給ポンプを設けると,その供給量で処理量を決定することが出来る。パス方式においてはタンク4Aと4Bの減圧度の差によって処理量が決定することが出来るが,メジアミルの構造によってはローターの回転数が上がると処理量が増すものもある。例えばSCミルは,ローターの回転に伴う負圧の発生によって吸引効果が生じるためにローターの回転数が上がると処理量が増す。但し,本発明においてメジアミルとして好適なスパイクミルの構造では,回転に伴う吸引力が働かないので,圧力差が支配要因となる。
【0049】
本発明の顔料分散装置として,少なくとも回収タンク4Bの一部に超音波発振器を設置した顔料分散装置は,メジアミルによって減圧分散処理された分散液の分散安定性をさらに向上させる。上記装置1Bは,タンク4A,4Bの両方に超音波発振器を設けた,好ましい形態を示してある。
【0050】
また,本発明の顔料分散装置の循環系を一定温度に保ったり,分散により固体顔料と液媒体との混合物または安定な分散液が必要以上に加熱されるのを避けるに当たって,メジアミルの分散部分,配管,タンクの少なくとも一部を冷却構造にした本発明の顔料分散装置は,減圧による,固体顔料と液媒体との混合物または安定な分散液中の揮発成分の蒸発を防止することも出来る。
【0051】
このジャケット構造は,固体顔料と液媒体との混合物または安定な分散液が接する部分になるべく広く設置されることが好ましく,また,冷却に伴う,装置各部の結露や凍結及び機械的な強度低下等の生じないような対策を行うことが好ましい。
【0052】
本発明では,少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含む顔料分散装置を用いて,固体顔料を液媒体に安定分散させるに当たり,当該混合物を循環させて,減圧下で,固体顔料を液媒体に安定分散させる。
【0053】
本発明では,固体顔料と液媒体とを必須成分として,分散を行うべき処理液たる,混合物が調製される。
【0054】
本発明の顔料分散方法に用いる固体顔料は,特に限定されるものではなく,公知慣用の顔料がいずれも使用できるが,例えばカーボンブラック,チタンブラック,チタンホワイト,硫化亜鉛,ベンガラ等の無機顔料や,フタロシアニン顔料,モノアゾ系,ジスアゾ系等のアゾ顔料,フタロシアニン顔料,キナクリドン顔料,イソインドリン顔料,ペリレン顔料,イミダゾロン顔料等の有機顔料などがある。
【0055】
この混合物には,固体顔料と液媒体の他に,樹脂や樹脂の中和剤を含めることが出来る。液媒体としては,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体が好適に用いられる。
【0056】
本発明の顔料分散方法において用いる樹脂も,特に限定はなく公知公用のものが使用可能であり,天然樹脂や合成樹脂に限定されず様々な樹脂が用いることができ,例えばスチレン系樹脂,(メタ)アクリル系樹脂,ポリエステル系樹脂,ポリウレタン系樹脂等が挙げられる。
【0057】
本発明のより好ましい樹脂としては,酸価を有する樹脂があり,塩基との組み合わせで水溶性あるいは水分散性の酸価を有する樹脂である。好ましい樹脂の酸価は,10〜200で,分子量は1000以上10万以下である。特に好ましい樹脂組成としてはスチレン,置換スチレン,(メタ)アクリル酸エステルからなる群から選ばれる少なくとも一つのモノマーと,(メタ)アクリル酸との共重合体である。
【0058】
本発明で用いる塩基としては,例えば水酸化ナトリウム(カセイソーダ),水酸化カリウム,水酸化リチウム等のアルカリ金属の水酸化物,アンモニア,トリエチルアミン,モルホリン等の塩基性物質の他,トリエタノールアミン,ジエタノールアミン,N−メチルジエタノールアミン等のアルコールアミンが使用可能であり,これらは単独あるいは組み合わせても良い。使用する塩基の量は,樹脂の酸基に対して分散性や,例えばインクジェット適性を考慮して適当な中和率に設定すればよい。
【0059】
液媒体は,この固体顔料を分散させるべき分散媒であり,水及び/又は有機溶剤が挙げられる。
【0060】
本発明の顔料分散方法において用いる有機溶剤として,前記した樹脂を溶解可能な水溶性有機溶剤が用いられるが,例えばアセトン,ジメチルケトン,メチルエチルケトン等のケトン系溶媒,メタノール,エタノール,イソプロピルアルコール等のアルコール系溶媒,酢酸エチルエステル等のエステル系溶媒,エチレングリコールモノメチルエーテル,エチレングリコールジメチルエーテル等のグリコールエーテル系溶媒,アミド類,等樹脂に合わせて選択すれば良い。これらの溶剤は,単独又は複数の組み合わせで樹脂を溶解又は分散するものがよい。
【0061】
一般の顔料分散,特に分散媒として有機溶剤が主の場合には,分散媒は顔料の中に容易に浸透しやすく,顔料を十分に濡らすことができる。一方,水若しくは水を主体とする液媒体においては強力な磨砕力を有するミルを用いてもなかなか顔料を濡らすことが難しい。
【0062】
本発明の顔料分散装置を用いて,少なくとも固体顔料と液媒体とからなる混合物の分散を行うと,顔料微粒子は,液媒体を構成する樹脂・有機溶剤・界面活性剤等によって,極めて効率良く濡れることになる。
【0063】
固体顔料を水若しくは水を主体とする液媒体に安定分散するに当たっては,界面活性剤等を用いる方法があるが,これらは,インキや塗料等の顔料分散液の最終使用用途において,皮膜耐水性などの点で,不都合を生じる場合が多い。
【0064】
本発明の顔料分散装置及び顔料分散方法は,界面活性剤を用いず,水若しくは水を主体とする分散媒への,固体顔料の安定分散を行うのに好適である。
【0065】
上記した様な,酸価を有する樹脂と塩基とを組み合わせて用いることにより,界面活性剤を用いずに,固体顔料の分散を行うことが出来,分散安定性に優れた顔料分散液を得ることが出来る。
【0066】
本発明の顔料分散方法では,本発明の分散装置によって,固体顔料を含む混合物がメジアミルによる分散中に減圧下にあると,少なくとも酸価を有する樹脂と水と,塩基からなる分散媒が,固体顔料の磨砕と共に生じる新たな顔料表面に極めて効率良く浸透し,その結果,固体顔料表面が濡れる。この時,より高い減圧度で分散を行う場合には,水などの沸点の低い分散媒成分の揮発を押さえて顔料分散液の組成が変化しないように,減圧度に応じた冷却を行うことが好ましい。
【0067】
本発明の顔料分散装置を用いて,少なくとも固体顔料と水のみ或いは水を主体とする液媒体からなる混合物の分散を行うと,顔料微粒子は分散媒を構成し得る,例えば酸価を有する樹脂・有機溶剤・塩基等によって極めて効率良く濡れることになる。
【0068】
その結果,得られた顔料分散液中の顔料微粒子は分散媒と完全に濡れることによって,より分散安定性に優れる。この顔料分散液は,例えばインクジェット記録用インクに用いると,安定したインクの吐出と鮮やかで優れた印刷品質が可能となる。
【0069】
液媒体として,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体を用いて,前記した操作を行うと,一部の樹脂は固体顔料の微粒子に吸着せず,分散媒中に溶解している場合が多いが,樹脂に対する貧溶媒を加えることによって,液媒体中の固体顔料の微粒子表面を,前記樹脂で被覆することが出来る。
【0070】
尚,樹脂に対する貧溶媒としては,水及び/または樹脂を溶解しない水溶性有機溶剤を用いるのが好ましい。これは水のみであっても,前記水溶性有機溶剤の水溶液であっても良い。
【0071】
本発明の顔料分散方法において,樹脂に対して貧溶媒として作用する有機溶剤は,水の他に,例えばエチレングリコール,プロピレングリコール,ジエチレングリコール,ジプロピレングリコール,ポリエチレングリコール,ポリプロピレングリコール,グリセリン等の多価アルコール類またはそれらのアルキルエーテル類等の水溶性有機溶剤及びそれらの水溶液がある。
【0072】
本発明の顔料分散方法での水と,水溶性有機溶剤の比率は,本発明における効果を達成すれば特に規定されないが,水/有機溶媒の重量比が10/1〜1/1となるような量が好ましい。
【0073】
上記した操作の結果,得られた顔料分散液中の顔料微粒子は分散媒との完全な濡れに加えて,樹脂による被覆が完全に行われることによって,極めて分散安定性に優れる。この顔料分散液はインクジェット記録用インクに用いると,より安定したインクの吐出と,より鮮やかでより優れた印刷品質を可能にする。
【0074】
特に,少なくとも,樹脂が酸価を有する樹脂と,水と,樹脂が自己水分散性になるように添加量をコントロールした,樹脂を溶解可能な水溶性有機溶剤と,塩基を含む液媒体は,本発明の顔料分散装置と顔料分散方法によって,自己水分散性となった樹脂が顔料微粒子表面を強力に被覆し,かつ,貧溶媒として,水のみ,または,樹脂を溶解しない水溶性有機溶剤の水溶液の様な,水を主体とする液媒体を加えることにより,液媒体に一部溶解している樹脂が,更に顔料微粒子表面を被覆し,いわゆるマイクロカプセルとなり極めて安定した着色樹脂粒子分散液となる。本発明では,このマイクロカプセルからなる着色樹脂粒子分散液も,顔料分散液と呼ぶ。
【0075】
この着色樹脂粒子分散液は,インクジェット記録用インクに用いると,最も優れた特性を発揮し,安定したインクの吐出と鮮やかで優れた印刷品質が,更に一層可能となる。
【0076】
本発明の顔料分散方法において,本発明の顔料分散装置による分散の前後に,固体顔料と液媒体との混合物や,顔料分散液について,他の分散手段による予備分散や後処理分散を行うことができる。
【0077】
上記の顔料分散方法における固体顔料と液媒体との混合物や,顔料分散液について,添加剤として,必要に応じて分散剤,可塑剤,酸化防止剤,紫外線吸収剤等を用いても良いし,これらは,本発明の顔料分散方法の任意の工程で加えても良い。
【0078】
この様にして本発明によって,所望の粒子径の顔料分散液が得られるが,通常その平均粒子径範囲は,0.01〜1μmである。尚,分散液を最終的に,例えばインクジェット用記録液として用いる場合には,平均粒子径をサブミクロンオーダー(1μm未満)とすればよい。
【0079】
この様にして得られた顔料分散液はそのまま用いることもできるが,共存している有機溶媒の影響で顔料粒子や着色樹脂粒子の分散安定性が悪い場合には,保存安定性をより向上させるためや,或いはより火災や公害に対する安全性を高めるために,更に脱溶媒を行うことが好ましい。
【0080】
この操作は,液媒体が,酸価を有する樹脂と,水と,樹脂溶解可能な水溶性有機溶剤と,塩基からなり,かつ,水及び/又は樹脂を溶解しない水溶性有機溶剤からなる前記樹脂に対する貧溶媒を加えて,液媒体中の固体顔料を前記樹脂で被覆して,固体顔料を被覆して液媒体に安定分散させた後に,少なくとも樹脂溶解可能な水溶性有機溶剤を液媒体から除去することにより実施できる。
【0081】
本発明の顔料分散方法によって得られる,サブミクロンオーダーの顔料マイクロカプセルを含む着色樹脂粒子分散液は,インクジェット記録用水性インクとして用いると,分散安定性,噴射特性に優れたインクジェット適性を示す。
【0082】
最終的に得られる着色樹脂粒子分散液をインクジェット記録用水性インクとして用いる場合には,本発明の各工程或い付加的に行われる工程の全てにおいて,液媒体は,イオン交換水以上の純度を有することが好ましい。
【0083】
また上記で得られた分散液を,インクジェット記録用インクとして用いる場合には,インクの乾燥を防止するために,乾燥防止剤を当該インク中に存在させておくのが好ましい。当該乾燥防止剤は,顔料分散液あるいは着色樹脂粒子分散液に直接添加すれば良い。
【0084】
かかる乾燥防止剤は,インクジェットの噴射ノズル口でのインクの乾燥を防止する効果を与えるものであり,通常水の沸点以上の沸点を有するものが使用される。このような乾燥防止剤としては,従来知られている公知慣用のものがいずれも使用できるが,例えばエチレングリコール,プロピレングリコール,ジエチレングリコール,ジプロピレングリコール,ポリエチレングリコール,ポリプロピレングリコール,グリセリン等の多価アルコール類またはそれらのアルキルエーテル類,等がある。
【0085】
乾燥防止剤の使用量は,種類によって異なるが,通常,水100重量部に対して1〜150重量部の範囲から適宜選択される。
【0086】
特に本発明の方法を,インクジェット記録用水性インクの製造方法に適用する場合においては,必要に応じて,インクを紙によりよく浸透させるための浸透性付与剤として,浸透性付与効果を示す水溶性有機溶媒,水溶性樹脂,pH調整剤,分散・消泡・紙への浸透のための界面活性剤,防腐剤,キレート剤等の添加剤を加えることができる。
【0087】
特に本発明の方法を,インクジェット記録用水性インクの製造方法に適用する場合においては,得られた分散液はそのまま水性インクとして用いることが出来るが,通常は,所望の粒径のフィルターに通過させ濾過して,インクジェット記録装置のノズル径よりも小さい粒子のみが液媒体に分散したインクジェット記録用水性インクとして使用に供される。従って,この用途の場合には,好ましくは最終濾過後に添加剤を添加するのは,避けたほうがよい。
【0088】
本発明の顔料分散方法によって得られる顔料マイクロカプセルからなる着色樹脂粒子は,分散液の状態で,或いは乾燥した固体及び粉体の状態で,発色性,分散安定性に優れていることから,インクジェット記録用水性インクの他,筆記具用インク,塗料,カラーフィルター,トナーへの応用が可能である。
【0089】
【発明の実施の形態】
本発明は次の実施形態を含む。
1. 少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含み,固体顔料が液媒体に安定分散するまで,当該容器と分散機構との間に,当該混合物を連続的に循環させる機構を設けたことを特徴とするメジアミルからなる顔料分散装置。
【0090】
2. 固体顔料と液媒体との混合物が通過する,運動するメジア群を含む前記分散機構が,ベッセルの内壁に微小間隙を介して,外壁を有する回転可能なロータを有し,その微小間隙にメジアが運動可能となる様に充填されており,ロータを回転させるとともに,固体顔料と液媒体との混合物を,分散機構中で略栓流となる様にして通過させる上記1記載の顔料分散装置。
【0091】
3. 固体顔料と液媒体との混合物を略栓流とするために,ロータ表面に,メジアに回転と衝撃力を与える突起と,当該混合物の流れ方向とは逆方向にメジアが戻される様に溝を形成した上記2記載の顔料分散装置。
【0092】
4. 固体顔料と液媒体との混合物を供給する供給容器,及び/又は,固体顔料が液媒体に安定分散した顔料分散液を回収する回収容器を有し,すくなくともいずれか一方から減圧を行う様にした上記1〜3記載の顔料分散装置。
【0093】
5. 供給容器と回収容器とを同一とした上記4記載の顔料分散装置。
【0094】
6. 供給容器と回収容器とを別々に両方有し,供給容器の圧力に対して,回収容器の圧力が負圧になるようにした上記4記載の顔料分散装置。
【0095】
7. 容器の一部に超音波発信機構を設けた上記1〜6記載の顔料分散装置。
【0096】
8. 分散液を冷却可能なように,少なくとも装置の一部が冷却構造を設けた上記1〜7記載の顔料分散装置。
【0097】
9. 少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含む顔料分散装置を用いて,固体顔料を液媒体に安定分散させるに当たり,当該混合物を循環させて,減圧下で,固体顔料を液媒体に安定分散させることを特徴とする顔料分散方法。
【0098】
10. 液媒体として,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体を用いる上記9記載の顔料分散方法。
【0099】
11. 液媒体として,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体を用い,前記樹脂に対する貧溶媒を加えて,液媒体中の固体顔料を前記樹脂で被覆して,固体顔料の微粒子表面を被覆して液媒体に安定分散させる上記9記載の顔料分散方法。
【0100】
12. 液媒体が,酸価を有する樹脂と,水と,樹脂溶解可能な水溶性有機溶剤と,塩基からなり,かつ,樹脂に対する貧溶媒が,水または樹脂を溶解しない水溶性有機溶剤である上記10または11記載の顔料分散方法。
【0101】
13.液媒体が,酸価を有する樹脂と,水と,樹脂溶解可能な水溶性有機溶剤と,塩基からなり,かつ,水または樹脂を溶解しない水溶性有機溶剤の水溶液からなる前記樹脂に対する貧溶媒を加えて,液媒体中の固体顔料を前記樹脂で被覆して,固体顔料を被覆して液媒体に安定分散させた後に,少なくとも樹脂溶解可能な水溶性有機溶剤を液媒体から除去する上記10または11記載の顔料分散方法。
【0102】
本発明は次の好ましい実施形態を含む。
(1)少なくとも分散が行われる部分が減圧構造を有し,かつ分散液が連続的に通過するメジアミルである顔料分散装置で,好ましくは,分散液の供給及び/又は回収タンクから減圧を行う。供給タンクと回収タンクを同一の供給兼回収タンクとして,減圧ラインを該タンクに設置するか,供給タンクと回収タンクを個別に設置する場合には,供給タンク側を常圧か減圧に設定し,さらに供給タンクの圧力に対して,回収タンクの圧力を負圧になるようにする。
【0103】
(2)顔料分散方法
少なくとも分散が行われる分散部分が,減圧構造を有するメジアミル(好適には,スパイクミルの供給兼回収タンクに減圧ライン)を用いて減圧しながら,顔料と,酸価を有する樹脂の塩基(好適にはカセイソーダ)を含む水溶液を用いて顔料分散を行う。
【0104】
(3)着色樹脂粒子分散液製造方法
少なくとも分散が行われる分散部分が,減圧構造を有するメジアミル(好適にはスパイクミルの供給兼回収タンクから減圧)を用いて減圧しながら,顔料と酸価を有する樹脂の塩基(好適には,樹脂の酸価に対して当量未満相当量のカセイソーダ)とメチルエチルケトンを含む水溶液を用いて顔料分散を行う。得られた顔料分散液に減圧下で撹拌しながら貧溶媒である水を滴下した後,メチルエチルケトンを留去して,顔料分散液のなかでも好適な着色樹脂粒子分散液を得る。
【0105】
本発明の好適な実施の形態を,インクジェット記録用インクに適用した場合を例にして説明すると,以下の通りである。
【0106】
得られた顔料分散液(好適には着色樹脂粒子分散液)に,インク調整用薬剤を加え,濃度・物性を調整した後,ろ過を行いインクジェット記録用水性インクとする。以上の操作は減圧下で行うことが好ましい。
【0107】
【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,以下の実施例中における「部」は『質量部』を表わす。
【0108】
(実施例1)
カ−ボンブラック20部とスチレン−アクリル酸−メタクリル酸樹脂(スチレン/アクリル酸/メタクリル酸=77/10/13;分子量7400・酸価160)10部を,水200部,カセイソーダ1部,の混合溶液に入れ,室温で分散撹拌機を用いて3時間撹拌し予備分散液を得た。
【0109】
直径0.3mmのジルコニアビーズを分散メヂアとした,井上製作所製のスパイクミルを準備し,上記で得られた予備分散液を,供給兼回収タンクに入れ,タンク及び配管全体を5℃に冷却しながら,30mmHgに減圧して8時間連続分散を行い,顔料分散液として,顔料マイクロカプセルを含む黒色着色樹脂粒子分散液を得た。尚,顔料分散に当たり,装置は図1に示す通りに構成した。
【0110】
得られた黒色分散液100部を,ジエチレングリコール20部,プロピレングリコールプロピルエーテル5部,水75部からなる水溶液に,撹拌しながら少しずつ加え,30mmHgで4時間撹拌を行い,0.5μmフィルターを用いて減圧ろ過を行い,インクジェット記録用水性インクとした。
【0111】
得られた水性インク中のマイクロカプセルは0.09μmの平均粒子径を有しており,凝集物もなく長期にわたって安定な分散を示し,サーマルジェット式インクジェットプリンターを用いた印字は安定しており,得られた印刷物は滲みもなく高い黒色度を示した。得られた印刷物は文字が乱れもなく,印刷濃度も高かった。
【0112】
(実施例2)
カ−ボンブラック20部とスチレン−アクリル酸−メタクリル酸樹脂(スチレン/アクリル酸/メタクリル酸=77/10/13;分子量5万・酸価160)20部を,水210部,グリセリン35部,トリエタノールアミン8部,メチルエチルケトン90部,イソプロピルアルコール40部の混合溶液に入れ,室温で分散撹拌機を用いて4時間撹拌し予備分散液を得た。
【0113】
直径0.3mmのジルコニアビーズを分散メヂアとした,井上製作所製のスパイクミルを準備し,上記で得られた予備分散液を,供給兼回収タンクに入れ,タンク及び配管全体を5℃に冷却しながら,30mmHgに減圧して8時間連続分散を行い,顔料分散液として,顔料マイクロカプセルを含む黒色着色樹脂粒子分散液を得た。尚,顔料分散に当たり,装置は図1に示す通りに構成した。
【0114】
得られた黒色分散液に30mmHgで減圧撹拌しながら,グリセリン30部と水210部の混合液を毎分5mlの速度で滴下し,その後ロータリーエバポレーターを用いてメチルエチルケトンとイソプロピルアルコールを留去し,さらに濃縮を行い,カーボンブラック含有量8%の最終の黒色着色樹脂粒子分散液を得た。
【0115】
得られた水分散物100部を,グリセリン20部,プロピレングリコールプロピルエーテル5部,水75部を加え30mmHgで4時間撹拌を行い,0.5μmフィルターを用いて減圧ろ過を行い,インクジェット記録用水性インクとした。
【0116】
得られた水性インク中のマイクロカプセルは0.09μmの平均粒子径を有しており,凝集物もなく長期にわたって安定な分散を示し,ピエゾ式インクジェットプリンターを用いた連続印字は安定しており,得られた印刷物は滲みもなく高い黒色度を示し,しかも耐水耐光性に優れていた。
【0117】
【発明の効果】
本発明の分散装置を用いた顔料分散方法によって得られる顔料分散液,着色樹脂粒子製造方法によって得られる着色樹脂粒子分散液は,微粒子径で,極めて分散安定性に優れており,インクジェット記録用水性インクに適用すると,分散安定性に優れ,安定したインクジェット吐出特性と優れた印刷品質を可能にする。
【図面の簡単な説明】
【図1】 本発明の供給タンクと回収タンクが同一である,減圧構造を有するメジアミル。
【図2】 本発明の供給タンクの圧力に対して,回収タンクの圧力が負圧になるような減圧構造を有するメジアミル。
【符号の説明】
1A 分散装置A
1B 分散装置B
2 ベッセルの壁
3 ローター
4 タンク
5 超音波発振器
6 脱気口
7 管
8 圧力調節弁
9 切替弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a pigment dispersion apparatus, a pigment dispersion method, and a colored resin particle dispersion production method capable of dispersing while reducing pressure. More specifically, the present invention relates to a dispersion device and a manufacturing method for a pigment of pigment ink for inkjet recording and a colored resin particle dispersion.
[0002]
[Prior art]
Ink jet recording inks are roughly classified into oil-based inks and water-based inks, but oil-based inks have problems in terms of odor and toxicity, and water-based inks are becoming mainstream.
[0003]
However, many of the conventional water-based inks have a drawback that water resistance and light resistance are poor because a water-soluble dye is used as a colorant. In addition, since the dye is dissolved at the molecular level, printing on so-called plain paper such as copy paper commonly used in offices causes bleeding called wrinkle-like feathering, which causes a significant decrease in print quality. .
[0004]
Various so-called water-based pigment inks have been proposed in the past to improve the above-mentioned drawbacks. For example, resin-dissolved inks in which carbon black or organic pigments are dispersed using a water-soluble resin as a binder / dispersant. Various resin-dispersed inks containing a colorant as polymer latex or microcapsules have been proposed.
[0005]
As water-based pigment inks for jet printers, colorant particles dispersed in a fine particle size as much as possible are required. As a specific example of a resin-soluble water-based ink, Japanese Patent No. 2512861 discloses (a) a pigment and Filling a 2-roll mill with a polymeric dispersant; (b) grinding to obtain a dispersion of pigment and polymeric dispersant; and (c) dispersing the pigment dispersion in an aqueous carrier medium A method for preparing an aqueous pigmented ink-jet ink having improved properties is disclosed in JP-A-3-153775 as follows: a) Solid pigment preparation b containing a pigment and a carboxyl group-containing polyacrylic resin b A water-based ink composition for ink jet printing has been proposed which contains a) an organic solvent dilutable with water c) a wetting agent d) water.
[0006]
Resin-dispersed water-based inks have the advantages of relatively little increase in viscosity due to water evaporation of the ink and excellent water resistance. Specifically, JP-A-58-45272 discloses an ink composition containing a urethane polymer latex containing a dye, and JP-A-62-95366 discloses a method in which a polymer and an oily dye are dissolved in a water-insoluble organic solvent. Furthermore, an ink containing a dye encapsulated in polymer particles by evaporating the solvent after mixing with an aqueous solution containing a surfactant and emulsifying is proposed. Japanese Patent Application Laid-Open No. Sho 62-254833 discloses an organic solvent for encapsulation. A method for producing an aqueous suspension of colorant by reducing the interfacial tension between water and water to 10 dynes or less has been proposed. In JP-A-1-170672, a recording liquid containing a macroencapsulated dye is similarly used. Has been proposed.
[0007]
However, although these techniques are effective for finer pigments, the dispersion stability of the dispersed colorant and the ejection stability from the nozzles are not always sufficient, and the printing quality is not always good.
[0008]
As means for improving the ejection stability of ink, known is a method under reduced pressure (vacuum) and / or ultrasonic treatment. Specifically, the recording liquid disclosed in JP-A-06-184479 is identified as an aqueous medium. A method in which at least one azo dye is sufficiently mixed and dissolved, pressure-filtered with a Teflon filter having a pore size of 1 μm, and degassed with a vacuum pump and an ultrasonic cleaner, Japanese Patent Laid-Open No. 06-25574 Ink jet printer inks include inks containing a finely dispersed three-phase suspension consisting of a continuous liquid phase, a discontinuous phase and a solid phase, specifically, for example, a solid phase consisting of a pigment such as carbon black. Stirring a hydrophilic phase containing triethanolamine, an emulsifying aid and water as an emulsifier in a hydrophobic phase containing a fine dispersion dispersed in oleic acid and an sorbitan monostearate as an emulsifying aid After the addition, the obtained suspension is subjected to ultrasonic treatment to obtain the above-mentioned three-phase suspension, and the recording liquid treatment method disclosed in Japanese Patent Application Laid-Open No. 09-286943 includes at least a dispersant, an aqueous liquid. A method of performing ultrasonic treatment and vacuum defoaming treatment after preparing and purifying an aqueous pigment-based recording liquid composed of a medium, a pigment, and water is disclosed.
[0009]
However, these technologies do not have the pigment dispersion effect of the ultrasonic wave itself, and the pigment dispersion stability and jet stability from the nozzle are small because the effect of finer pigment, improvement of wetting, and defoaming effect are small. However, the print quality was not always good.
[0010]
On the other hand, as a general pigment dispersion method, a coloring material for paint as disclosed in JP-A-61-163970 and as a method for producing the same, the pigment is wet treated with a solution containing a resin for paint, and the pigment is dispersed in the solution. Thereafter, a method of obtaining a coating colorant having excellent optical properties of the coating film by drying and solidifying and coating the pigment surface with a coating resin is disclosed in Japanese Patent Application Laid-Open No. 62-192471. In the manufacturing method, the pigment dispersibility is greatly improved by instantaneous vacuum drying of the dispersion in which the pigment is uniformly dispersed in the resin solution dissolved in the solvent by the wet disperser, and the hiding property and smoothness are excellent. A method for obtaining a powder coating material has been proposed and can be applied as a method for producing ink for ink jet recording. However, in order to solidify the dispersion once, a redispersion step is necessary. Wetting to dispersion medium Discharge stability of insufficient ink is insufficient.
[0011]
In addition, in the method for producing a magnetic paint disclosed in Japanese Patent Application Laid-Open No. 09-12933, a kneading step of kneading the magnetic paint using a continuous biaxial kneader is performed by kneading the kneading part of the kneader in a vacuum atmosphere. However, in the apparatus configuration of this manufacturing method, magnetic powder and paint resin are melt-kneaded, and wet-kneading is impossible.
[0012]
In general, it is known that pigment dispersion is performed under reduced pressure, but a pigment dispersion apparatus capable of performing pigment dispersion continuously and efficiently has not been known.
[0013]
[Problems to be solved by the invention]
The problem to be solved by the present invention is a pigment that enables an ink composition using a pigment as a colorant, which has excellent dispersion stability with fine particle size, and enables stable jetting and excellent print quality in ink jet recording. An object of the present invention is to provide a dispersing device, a pigment dispersing method, and a colored resin particle manufacturing method.
[0014]
[Means for Solving the Problems]
As a result of intensive studies in order to solve the above problems, the present inventors have solved the present invention. That is, the present invention provides the following inventions.
[0015]
(1) Pigment dispersing device
It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. A mechanism for continuously circulating the mixture between the vessel and the dispersion mechanism until the solid pigment is stably dispersed in the liquid medium. A pigment dispersion apparatus comprising mediamil.
[0016]
(2) Pigment dispersion method
It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. In order to stably disperse the solid pigment in the liquid medium by using a pigment dispersing apparatus including the mediamyl which disperses the solid pigment in the liquid medium, the mixture is circulated and the solid pigment is stabilized in the liquid medium under reduced pressure. A pigment dispersion method characterized by dispersing.
[0017]
Hereinafter, the present invention will be described in order.
[0018]
The pigment dispersion apparatus of the present invention is a pigment dispersion apparatus in which at least a part where dispersion is performed has a decompression structure and is a media mill through which the dispersion continuously passes, preferably a dispersion supply and / or recovery tank The pigment dispersion device is configured to perform decompression from the beginning.
[0019]
The pigment dispersing apparatus of the present invention has at least the following configuration.
{Circle around (1)} A container having a structure capable of depressurization for containing a mixture of a liquid medium (corresponding to a dispersion medium) and a solid pigment.
(2) It has a dispersion mechanism for passing and dispersing between moving media groups, and has a media mill for dispersing the solid pigment in the liquid medium, enabling the portion where the solid pigment is dispersed in the liquid medium to be decompressed.
(3) A mechanism for continuously circulating the mixture (1) between the container (1) and the dispersion mechanism until the solid pigment is stably dispersed in the liquid medium.
[0020]
The greatest feature of the pigment dispersing apparatus of the present invention is that it has both the above (1) and (3).
[0021]
As the media mill which is a preferred dispersing apparatus of the present invention, any of the known and conventional bead mills and ball mills can be used. For example, the passing type is classified according to an introduction to dispersion technology (Nikkan Kogyo Shimbun; written by Masumi Koishi and Taiichi Tsuritani). Mills (sand mills, continuous attritors, pearl mills, Molinex) and their deformation mills (Dryswerke DCP mills, Mitsui Mining SC mills, Inoue Spike mills, Shinmaru Enterprises dyno mills ECM, Asada Tekko nano mills Etc.).
[0022]
These are dispersing devices that grind and disperse the pigment by utilizing the grinding shear force of the dispersed media (ball or bead). In the present invention, these are used so that they can be performed under reduced pressure.
[0023]
Among them, the dispersion mechanism including a moving media group through which a mixture of a solid pigment and a liquid medium passes has a rotatable rotor having an outer wall through a minute gap on the inner wall of the vessel, An annular media mill that is filled so that the media can be moved, rotates the rotor, and allows the mixture of the solid pigment and the liquid medium to pass through the dispersion mechanism in a substantially plug flow. Is particularly preferred.
[0024]
In order to make the mixture of the solid pigment and the liquid medium into a stable solid pigment dispersion, in order to make the mixture substantially plug flow, in addition to the above, for example, a rotation and impact force is applied to the media on the rotor surface. It is preferable to form a groove so that the projection and the median are returned in the direction opposite to the flow direction of the mixture.
[0025]
It is preferable to provide a cooling structure in at least a part of the apparatus so that the mixture of the solid pigment and the liquid medium or the solid pigment dispersion can be cooled. Specifically, a cooling jacket is provided inside the rotor or the outer wall of the vessel so as not to come into direct contact with the mixture of the solid pigment and the liquid medium or the solid pigment dispersion, and a coolant such as cooling water is passed through. It is preferable to adjust the temperature during dispersion. Hereinafter, such a particularly preferred media mill is referred to as a spike mill.
[0026]
A small gap between the rotor and the vessel of the media mill is filled with a media for dispersion. Existing dispersion media can be used for the dispersion of the present invention. The finer the media diameter, the higher the density, and the higher the rotation speed, the higher the pigment grinding ability. The dispersed media is preferably glass beads, ceramic beads, steel balls, stainless balls, cross-linked resin beads, and the like. In order to make the pigment into fine particles, beads having a diameter as small as possible are preferable. These media are not allowed to flow out of the media.
[0027]
In the present invention, a container having a structure capable of depressurization for containing a mixture of a solid pigment and a liquid medium is provided. However, a supply container for supplying a mixture of the solid pigment and the liquid medium and / or the solid pigment is supplied to the liquid medium. It has a collection container that collects the stably dispersed pigment dispersion, and the pressure is reduced from at least one of them.
[0028]
That is, in the present invention, there are a case where the supply container and the recovery container are the same and only one is used as a dual-purpose container, and a case where both the supply container and the recovery container are used separately. In the former case, it is preferable that the pressure is reduced from this single combined container, and in the latter case, the pressure is reduced so that the pressure of the recovery container becomes negative with respect to the pressure of the supply container.
[0029]
In addition, it is preferable to provide an ultrasonic transmission mechanism in a part of the container in that a stable dispersion can be obtained in a shorter time when the same media mill is operated under the same operating conditions.
[0030]
A mechanism for continuously circulating a mixture of the solid pigment and the liquid medium is provided between the containers and the dispersion mechanism until the solid pigment is stably dispersed in the liquid medium. Specifically, this mechanism can be provided by providing tubes and connecting them. Of course, it is also possible to provide a jacket in this piping portion so as to adjust the temperature during dispersion in the same manner as described above, and it is preferable to actually do so.
[0031]
For example, degassing may be performed to reduce the pressure in the portion where the media diamyl is dispersed. If the vessel and the pipe are connected to each other, for example, a mixture of a solid pigment and a liquid medium may be put in, and the pressure may be reduced from above the vessel having a depressurizable structure.
[0032]
The dispersion temperature and pressure for carrying out the pigment dispersion method of the present invention are not particularly limited and may be appropriately selected. As the dispersion temperature, the entire circulation system is 1 to 20 ° C., preferably 1 The circulating system pressure is 1 to 500 mmHg, preferably 1 to 100 mmHg. In the case of obtaining a pigment dispersion for water-based ink for ink jet recording, the circulation system in which the dispersion is performed has a temperature of 1 to 5 in that the printing density is higher and stable, and the ejection stability in long-term continuous printing is better. It is particularly preferable that the pressure is 1 to 100 mmHg at 10 ° C.
[0033]
Using such a pigment dispersion apparatus, the mixture is repeatedly circulated until a stable solid pigment dispersion is obtained, thereby dispersing the solid pigment in the liquid medium. In order to obtain a stable dispersion, it is necessary to perform sampling under various conditions in the middle of the circulation in advance, find conditions that maintain the required stability, and then carry out under the optimum conditions. preferable. In general, it is preferable to perform processing until the dispersion stability becomes constant and becomes saturated.
[0034]
Next, the pigment dispersion apparatus of this invention is demonstrated using drawing. FIG. 1 shows a pigment dispersion apparatus 1A having a decompression structure in which the supply tank and the recovery tank of the present invention are the same. The black arrow indicates the flow direction of the mixture with the liquid medium of the solid pigment, and the white arrow indicates the flow direction in the jacket (described later) through which the liquid medium for maintaining the apparatus at a constant temperature is passed (hereinafter referred to as the flow direction). , And so on.)
[0035]
This apparatus corresponds to a container having a depressurizable structure, which is a supply container / collection container provided with a deaeration pump (not shown) corresponding to a deaeration element and a deaeration port 6 that needs to be depressurized. And a pipe 7 for connecting the tank 4 and the media mill, which is a mechanism for continuously circulating a mixture of the liquid medium of the media pigment and the media pigment. In actual use, the deaeration pump and the deaeration port 6 are connected by a pipe to bring the system into a depressurized state.
[0036]
An ultrasonic oscillator 5 corresponding to an ultrasonic transmission mechanism is provided on a side portion inside the tank 4. On the other hand, a pipe 4 on the side for supplying a mixture of the tank 4 and a liquid medium of a solid pigment is provided. A jacket is provided outside to keep the circulation system at a constant temperature. The lower part of the tank 4 is connected to the inlet (inlet port) of the media mill by a pipe 7. On the contrary, the outlet (discharge port) of the media mill is connected by a pipe 7 so as to be returned to the tank 4 and thereby circulates.
[0037]
When supplying the mixture of the solid pigment and the liquid medium more stably to the inlet of the media mill, although not shown, a supply pump may be provided.
[0038]
The media mill includes a vessel and the rotor 3, and has a minute gap between the vessel wall 2 and the outer wall of the rotor 3, and the gap is filled with the dispersed media. This rotor is annular and rotates about its axis. When the mixture of the solid pigment and the liquid medium is introduced from the inlet of the media mill through the pipe 7 and passed through this gap, the rotor 3 rotates. The media group moves, and the shearing force causes dispersion of the solid pigment into the liquid medium, so that the dispersion state is more stable than the inlet, and is discharged to the pipe 7 from the outlet (discharge port) of the media mill. It has become. The surface of the rotor 3 is provided with irregularities so that the momentum based on the rotation and impact force of the media is increased and, as a result, a large shearing force acts on the mixture.
[0039]
Similarly, a jacket is provided outside the vessel so that the temperature inside the system can be kept constant even when passing through a minute gap.
[0040]
By doing so, it becomes possible to circulate and disperse the mixture or a dispersion liquid still having insufficient dispersion stability while reducing the pressure.
[0041]
FIG. 2 shows a pigment dispersion apparatus 1B having a decompression structure, which has both the supply container and the recovery container of the present invention separately. This apparatus 1B has a supply tank 4A corresponding to the supply container and a recovery tank 4B corresponding to the recovery container, and each tank has a deaeration port 6 and an ultrasonic oscillator 5 as in the apparatus 1A. Each is provided. Further, a pressure control valve 8 is provided in a part of the pipe 7 connecting the tank 4A and the media mill, and a switching valve 9 is provided in a part of the pipe 7 connecting the tanks 4A and 4B.
[0042]
In the case of this apparatus 1B, the pressure of the recovery tank 4B is negative with respect to the pressure of the supply tank 4A, that is, 4B is higher in pressure than the tank 4A. It is preferable to disperse the solid pigment in the liquid medium.
[0043]
Specifically, when the supply tank 4A and the recovery tank 4B are individually installed as described above, the supply tank 4A side is set to normal pressure or reduced pressure, and further, the recovery tank 4B is set against the pressure of the supply tank 4A. By making the pressure of the negative pressure, it is possible to disperse under reduced pressure in the dispersion part in the media mill. Valves 8 and 9 are used for pressure adjustment at this time.
[0044]
At this time, if a supply pump for supplying the mixture of the solid pigment and the liquid medium to the inlet of the media mill is provided, the load on the pump can be greatly reduced. Become. The mixture of the solid pigment and the liquid medium received in the supply tank 4A is once returned to normal pressure and then returned to the recovery tank, and is circulated and repeatedly dispersed again until the dispersion stability of the solid pigment in the liquid medium is saturated. Although it is possible to perform the dispersion, it is possible to continue the dispersion without returning to the normal pressure by returning the dispersion liquid to the supply tank with a suction pump having a pressure equal to or higher than that of the recovery tank 4B.
[0045]
At this time, it is preferable that the media mill is provided with a valve structure for generating pressure loss on the supply side of the dispersion portion, or the above deformation mill in which the cross-sectional area of the dispersion portion is small and large pressure loss is generated in the dispersion portion.
[0046]
In the case of the apparatus of FIG. 2, the mixture of the solid pigment filled in the tank 4A and the liquid medium is supplied into the vessel of the media mill by the pressure difference between the tank 4A and the tank 4B, but the pressure control valve 8 is throttled. Thus, the negative pressure in the vessel can be controlled. At this time, the switching valve 9 between the tank 4A and the tank 4B is closed.
[0047]
When the dispersion liquid of the mixture is collected in the tank 4B, the pressure control valve 8 is closed, and when the switching valve 8 is opened by reversing the pressure reduction of the tanks 4A and 4B, the mixture is transferred from the tanks 4A to 4B. Moving. By repeating the same operation for the mixture of the solid pigment and the liquid medium, it is possible to repeat the path dispersion. By repeating this process until the dispersion stability is saturated and a stable dispersion is obtained, the dispersion stability of the mixture is further improved.
[0048]
In the case of circulation dispersion, the flow rate or the processing amount of the mixture in the media mill can be determined by the supply amount provided with a supply pump. In the pass method, the processing amount can be determined by the difference in the degree of pressure reduction between the tanks 4A and 4B. However, depending on the structure of the media mill, the processing amount may increase as the rotor speed increases. For example, the SC mill has a suction effect due to the generation of negative pressure accompanying the rotation of the rotor, so that the throughput increases as the rotor speed increases. However, in the spike mill structure suitable as a media mill in the present invention, the suction force accompanying rotation does not work, so the pressure difference becomes the dominant factor.
[0049]
As a pigment dispersion apparatus of the present invention, a pigment dispersion apparatus in which an ultrasonic oscillator is installed at least in a part of the recovery tank 4B further improves the dispersion stability of a dispersion liquid subjected to a vacuum dispersion treatment by a media mill. The apparatus 1B is shown in a preferred form in which an ultrasonic oscillator is provided in both tanks 4A and 4B.
[0050]
Further, in order to keep the circulation system of the pigment dispersing apparatus of the present invention at a constant temperature, or to avoid excessive heating of the mixture of the solid pigment and the liquid medium or the stable dispersion due to the dispersion, The pigment dispersion apparatus of the present invention in which at least a part of the pipe and the tank has a cooling structure can also prevent evaporation of volatile components in the mixture of the solid pigment and the liquid medium or the stable dispersion due to the reduced pressure.
[0051]
This jacket structure is preferably installed as wide as possible where the mixture of solid pigment and liquid medium or stable dispersion comes into contact. Also, dew condensation and freezing of parts of the apparatus and mechanical strength decrease due to cooling. It is preferable to take measures to prevent this from occurring.
[0052]
In the present invention, the portion where the dispersion of the solid pigment into the liquid medium is performed, which has a container having at least a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium between the moving media groups. In order to stably disperse the solid pigment in the liquid medium using a pigment dispersing apparatus comprising a mediamyl which disperses the solid pigment in the liquid medium, the mixture is circulated and the solid pigment is circulated under reduced pressure. Disperse stably in a liquid medium.
[0053]
In the present invention, a mixture, which is a treatment liquid to be dispersed, is prepared using a solid pigment and a liquid medium as essential components.
[0054]
The solid pigment used in the pigment dispersion method of the present invention is not particularly limited, and any known and commonly used pigment can be used. For example, inorganic pigments such as carbon black, titanium black, titanium white, zinc sulfide, bengara, etc. , Phthalocyanine pigments, monoazo and disazo pigments, organic pigments such as phthalocyanine pigments, quinacridone pigments, isoindoline pigments, perylene pigments and imidazolone pigments.
[0055]
In addition to the solid pigment and the liquid medium, the mixture can contain a resin and a resin neutralizer. As the liquid medium, a liquid medium containing at least a resin having an acid value, water, and a base is preferably used.
[0056]
The resin used in the pigment dispersion method of the present invention is not particularly limited, and publicly known and public ones can be used, and various resins can be used without being limited to natural resins or synthetic resins. ) Acrylic resin, polyester resin, polyurethane resin and the like.
[0057]
More preferable resins of the present invention include resins having an acid value, and resins having a water-soluble or water-dispersible acid value in combination with a base. The acid value of the preferred resin is 10 to 200, and the molecular weight is 1000 or more and 100,000 or less. A particularly preferred resin composition is a copolymer of (meth) acrylic acid and at least one monomer selected from the group consisting of styrene, substituted styrene, and (meth) acrylic acid ester.
[0058]
Examples of the base used in the present invention include alkali metal hydroxides such as sodium hydroxide (caustic soda), potassium hydroxide and lithium hydroxide, basic substances such as ammonia, triethylamine and morpholine, triethanolamine and diethanolamine. , N-methyldiethanolamine and other alcohol amines can be used, and these may be used alone or in combination. The amount of the base to be used may be set to an appropriate neutralization rate in consideration of dispersibility with respect to the acid group of the resin, for example, ink jet aptitude.
[0059]
The liquid medium is a dispersion medium in which the solid pigment is to be dispersed, and examples thereof include water and / or an organic solvent.
[0060]
As the organic solvent used in the pigment dispersion method of the present invention, a water-soluble organic solvent capable of dissolving the above-described resin is used. For example, ketone solvents such as acetone, dimethyl ketone and methyl ethyl ketone, alcohols such as methanol, ethanol and isopropyl alcohol are used. The solvent may be selected according to the resin such as a solvent, an ester solvent such as ethyl acetate, a glycol ether solvent such as ethylene glycol monomethyl ether or ethylene glycol dimethyl ether, an amide or the like. These solvents are preferably those that dissolve or disperse the resin alone or in combination.
[0061]
In the case of general pigment dispersion, particularly when an organic solvent is mainly used as a dispersion medium, the dispersion medium easily penetrates into the pigment and can sufficiently wet the pigment. On the other hand, in the case of water or a liquid medium mainly composed of water, it is difficult to wet the pigment even if a mill having a strong grinding power is used.
[0062]
When a mixture of at least a solid pigment and a liquid medium is dispersed using the pigment dispersion apparatus of the present invention, the pigment fine particles are wetted very efficiently by the resin, organic solvent, surfactant, etc. constituting the liquid medium. It will be.
[0063]
In order to stably disperse a solid pigment in water or a liquid medium mainly composed of water, there is a method using a surfactant or the like. In many cases, such problems occur.
[0064]
The pigment dispersion apparatus and the pigment dispersion method of the present invention are suitable for stably dispersing a solid pigment in water or a dispersion medium mainly composed of water without using a surfactant.
[0065]
By using a combination of a resin having an acid value and a base as described above, a solid pigment can be dispersed without using a surfactant, and a pigment dispersion having excellent dispersion stability can be obtained. I can do it.
[0066]
In the pigment dispersion method of the present invention, when the mixture containing the solid pigment is under reduced pressure during dispersion by the media mill, the dispersion medium comprising at least an acid value resin, water, and a base is obtained by the dispersion apparatus of the present invention. It penetrates into the new pigment surface generated with the grinding of the pigment very efficiently, and as a result, the solid pigment surface gets wet. At this time, when dispersing at a higher degree of vacuum, cooling according to the degree of vacuum should be performed so that the composition of the pigment dispersion does not change by suppressing the volatilization of the dispersion medium component having a low boiling point such as water. preferable.
[0067]
When a mixture of at least a solid pigment and water or a liquid medium mainly composed of water is dispersed using the pigment dispersing apparatus of the present invention, the pigment fine particles can form a dispersion medium, for example, a resin having an acid value. It gets wet very efficiently by organic solvents and bases.
[0068]
As a result, the pigment fine particles in the obtained pigment dispersion are more excellent in dispersion stability by being completely wetted with the dispersion medium. When this pigment dispersion is used, for example, in ink for ink jet recording, stable ink ejection and vivid and excellent print quality are possible.
[0069]
When the above operation is performed using a liquid medium containing at least an acid value resin, water, and a base as a liquid medium, a part of the resin is not adsorbed on the fine particles of the solid pigment and is not contained in the dispersion medium. Although it is often dissolved, the surface of the fine particles of the solid pigment in the liquid medium can be coated with the resin by adding a poor solvent for the resin.
[0070]
As the poor solvent for the resin, it is preferable to use water and / or a water-soluble organic solvent that does not dissolve the resin. This may be water alone or an aqueous solution of the water-soluble organic solvent.
[0071]
In the pigment dispersion method of the present invention, the organic solvent that acts as a poor solvent for the resin is, in addition to water, a polyvalent such as ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol, and glycerin. There are water-soluble organic solvents such as alcohols or their alkyl ethers and their aqueous solutions.
[0072]
The ratio of water to the water-soluble organic solvent in the pigment dispersion method of the present invention is not particularly defined as long as the effect of the present invention is achieved, but the weight ratio of water / organic solvent is 10/1 to 1/1. A small amount is preferred.
[0073]
As a result of the operation described above, the pigment fine particles in the obtained pigment dispersion are extremely excellent in dispersion stability by being completely covered with the resin in addition to being completely wetted with the dispersion medium. When this pigment dispersion is used in ink for ink jet recording, it enables more stable ink ejection and more vivid and superior printing quality.
[0074]
In particular, a liquid medium containing at least a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, the amount of which is controlled so that the resin is self-dispersible, and a base, By the pigment dispersing apparatus and the pigment dispersing method of the present invention, the resin that has become self-water-dispersible strongly coats the surface of the pigment fine particles, and as a poor solvent, only water or a water-soluble organic solvent that does not dissolve the resin is used. By adding a liquid medium mainly composed of water, such as an aqueous solution, the resin partially dissolved in the liquid medium further coats the surface of the pigment fine particles to form a so-called microcapsule and a highly stable colored resin particle dispersion. Become. In the present invention, the colored resin particle dispersion comprising the microcapsules is also referred to as a pigment dispersion.
[0075]
When this colored resin particle dispersion is used in ink for ink jet recording, it exhibits the most excellent characteristics, and more stable discharge of ink and vivid and excellent print quality are possible.
[0076]
In the pigment dispersion method of the present invention, pre-dispersion or post-processing dispersion by other dispersion means may be performed on the mixture of the solid pigment and the liquid medium or the pigment dispersion before and after dispersion by the pigment dispersion apparatus of the present invention. it can.
[0077]
For the mixture of the solid pigment and the liquid medium in the above pigment dispersion method and the pigment dispersion, a dispersant, a plasticizer, an antioxidant, an ultraviolet absorber, etc. may be used as an additive, if necessary. These may be added at any step of the pigment dispersion method of the present invention.
[0078]
Thus, according to the present invention, a pigment dispersion having a desired particle size can be obtained, but the average particle size range is usually 0.01 to 1 μm. When the dispersion is finally used, for example, as an ink jet recording liquid, the average particle diameter may be on the order of submicrons (less than 1 μm).
[0079]
The pigment dispersion obtained in this way can be used as it is, but if the dispersion stability of pigment particles or colored resin particles is poor due to the coexisting organic solvent, the storage stability is further improved. In order to improve safety against fire or pollution, it is preferable to further remove the solvent.
[0080]
In this operation, the resin is composed of a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, a base, and a water-soluble organic solvent that does not dissolve water and / or the resin. After coating the solid pigment in the liquid medium with the above resin, coating the solid pigment and stably dispersing in the liquid medium, remove at least the water-soluble organic solvent that can dissolve the resin from the liquid medium. Can be implemented.
[0081]
The colored resin particle dispersion containing submicron-order pigment microcapsules obtained by the pigment dispersion method of the present invention exhibits inkjet suitability excellent in dispersion stability and jetting characteristics when used as an aqueous ink for inkjet recording.
[0082]
When the finally obtained colored resin particle dispersion is used as a water-based ink for ink jet recording, the liquid medium has a purity higher than that of ion-exchanged water in each step of the present invention or all of the additional steps. It is preferable to have.
[0083]
When the dispersion obtained above is used as an ink for inkjet recording, it is preferable that an anti-drying agent is present in the ink in order to prevent the ink from drying. The drying inhibitor may be added directly to the pigment dispersion or the colored resin particle dispersion.
[0084]
Such an anti-drying agent has an effect of preventing the ink from drying at the jet nozzle opening of the ink jet, and usually has a boiling point equal to or higher than the boiling point of water. As such an anti-drying agent, any conventionally known ones can be used. For example, polyhydric alcohols such as ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol, and glycerin. Or their alkyl ethers.
[0085]
The amount of the anti-drying agent used varies depending on the type, but is usually appropriately selected from the range of 1 to 150 parts by weight per 100 parts by weight of water.
[0086]
In particular, when the method of the present invention is applied to a method for producing a water-based ink for ink-jet recording, a water-solubility exhibiting a penetrability-imparting effect as a penetrability-imparting agent for allowing the ink to penetrate better into paper as required Additives such as organic solvents, water-soluble resins, pH adjusters, surfactants for dispersion, defoaming, and paper penetration, preservatives, and chelating agents can be added.
[0087]
In particular, when the method of the present invention is applied to a method for producing a water-based ink for ink-jet recording, the obtained dispersion can be used as a water-based ink as it is, but is usually passed through a filter having a desired particle size. It is filtered and used as a water-based ink for ink jet recording in which only particles smaller than the nozzle diameter of the ink jet recording apparatus are dispersed in a liquid medium. Therefore, for this application, it is preferable to avoid adding additives after the final filtration.
[0088]
The colored resin particles comprising the pigment microcapsules obtained by the pigment dispersion method of the present invention are excellent in color development and dispersion stability in the state of dispersion or in the state of dried solid and powder. In addition to recording water-based inks, it can be applied to writing instrument inks, paints, color filters, and toners.
[0089]
DETAILED DESCRIPTION OF THE INVENTION
The present invention includes the following embodiments.
1. It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. A mechanism for continuously circulating the mixture between the vessel and the dispersion mechanism until the solid pigment is stably dispersed in the liquid medium. A pigment dispersion apparatus comprising mediamil.
[0090]
2. The dispersion mechanism including a moving media group through which a mixture of a solid pigment and a liquid medium passes has a rotatable rotor having an outer wall through a minute gap on the inner wall of the vessel, and the media is located in the minute gap. 2. The pigment dispersion apparatus according to 1 above, which is filled so as to be movable, rotates the rotor, and allows the mixture of the solid pigment and the liquid medium to pass through the dispersion mechanism in a substantially plug flow.
[0091]
3. In order to make the mixture of the solid pigment and liquid medium substantially plug flow, the rotor surface is provided with protrusions that apply rotation and impact force to the media and a groove so that the media is returned in the direction opposite to the flow direction of the mixture. 3. The pigment dispersion apparatus as described in 2 above.
[0092]
4). A supply container for supplying a mixture of a solid pigment and a liquid medium and / or a recovery container for recovering a pigment dispersion in which the solid pigment is stably dispersed in the liquid medium are provided, and the pressure is reduced from at least one of them. The pigment dispersion apparatus of said 1-3.
[0093]
5). 5. The pigment dispersion apparatus according to 4 above, wherein the supply container and the recovery container are the same.
[0094]
6). 5. The pigment dispersion apparatus as described in 4 above, wherein both the supply container and the recovery container are provided separately, and the pressure of the recovery container is negative with respect to the pressure of the supply container.
[0095]
7). 7. The pigment dispersion apparatus according to 1 to 6 above, wherein an ultrasonic wave transmission mechanism is provided in a part of the container.
[0096]
8). 8. The pigment dispersion apparatus according to any one of 1 to 7 above, wherein at least a part of the apparatus is provided with a cooling structure so that the dispersion liquid can be cooled.
[0097]
9. It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. In order to stably disperse the solid pigment in the liquid medium by using a pigment dispersing apparatus including the mediamyl which disperses the solid pigment in the liquid medium, the mixture is circulated and the solid pigment is stabilized in the liquid medium under reduced pressure. A pigment dispersion method characterized by dispersing.
[0098]
10. 10. The pigment dispersion method according to 9 above, wherein a liquid medium containing at least an acid value resin, water, and a base is used as the liquid medium.
[0099]
11. A liquid medium containing at least a resin having an acid value, water, and a base is added as a liquid medium, a poor solvent for the resin is added, and the solid pigment in the liquid medium is coated with the resin, so that the solid pigment 10. The pigment dispersion method as described in 9 above, wherein the fine particle surface is coated and stably dispersed in a liquid medium.
[0100]
12 The liquid medium is composed of a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, and a base, and the poor solvent for the resin is a water-soluble organic solvent that does not dissolve water or the resin. Or the pigment dispersion method of 11.
[0101]
13. A poor solvent for the resin, wherein the liquid medium is composed of a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, and a base, and an aqueous solution of water or a water-soluble organic solvent that does not dissolve the resin. In addition, after the solid pigment in the liquid medium is coated with the resin, and the solid pigment is coated and stably dispersed in the liquid medium, at least the water-soluble organic solvent capable of dissolving the resin is removed from the liquid medium. 11. The pigment dispersion method according to 11.
[0102]
The present invention includes the following preferred embodiments.
(1) A pigment dispersion apparatus in which at least a portion where dispersion is performed has a decompression structure and is a media mill through which the dispersion continuously passes, preferably, the decompression is performed from the supply and / or recovery tank of the dispersion. When the supply tank and the recovery tank are the same supply and recovery tank and the decompression line is installed in the tank, or when the supply tank and the recovery tank are installed separately, the supply tank side is set to normal pressure or decompression, Furthermore, the recovery tank pressure is set to a negative pressure relative to the supply tank pressure.
[0103]
(2) Pigment dispersion method
At least the dispersion portion where the dispersion is performed is made by using a media mill having a decompression structure (preferably a decompression line to the supply and recovery tank of the spike mill) while reducing the pressure, and a pigment and a resin base having an acid value (preferably Pigment dispersion using an aqueous solution containing caustic soda).
[0104]
(3) Colored resin particle dispersion manufacturing method
At least the dispersion part where dispersion is performed is a base of a resin having a pigment and an acid value (preferably a resin, preferably while reducing pressure using a media mill having a reduced pressure structure (preferably reduced pressure from a supply and recovery tank of a spike mill). Pigment dispersion is carried out using an aqueous solution containing caustic soda) and methyl ethyl ketone in an equivalent amount less than the equivalent of the acid value. Water, which is a poor solvent, is added dropwise to the obtained pigment dispersion while stirring under reduced pressure, and then methyl ethyl ketone is distilled off to obtain a suitable colored resin particle dispersion among pigment dispersions.
[0105]
A preferred embodiment of the present invention will be described as an example where it is applied to an ink for ink jet recording.
[0106]
An ink adjusting agent is added to the obtained pigment dispersion (preferably colored resin particle dispersion) to adjust the concentration and physical properties, followed by filtration to obtain an aqueous ink for inkjet recording. The above operation is preferably performed under reduced pressure.
[0107]
【Example】
Next, the present invention will be described more specifically with reference to examples and comparative examples. In the following examples, “part” represents “part by mass”.
[0108]
Example 1
20 parts of carbon black and 10 parts of styrene-acrylic acid-methacrylic acid resin (styrene / acrylic acid / methacrylic acid = 77/10/13; molecular weight 7400 / acid value 160), 200 parts of water, 1 part of caustic soda, It put into the mixed solution and stirred for 3 hours using a dispersion stirrer at room temperature to obtain a preliminary dispersion.
[0109]
Prepare a spike mill manufactured by Inoue Seisakusho using zirconia beads with a diameter of 0.3 mm as dispersion media. Place the pre-dispersed liquid obtained above in the supply and recovery tank and cool the tank and the entire pipe to 5 ° C. Then, the pressure was reduced to 30 mmHg and continuous dispersion was performed for 8 hours to obtain a black colored resin particle dispersion containing pigment microcapsules as the pigment dispersion. In dispersing the pigment, the apparatus was configured as shown in FIG.
[0110]
100 parts of the obtained black dispersion was added to an aqueous solution consisting of 20 parts of diethylene glycol, 5 parts of propylene glycol propyl ether and 75 parts of water while stirring, and stirred at 30 mmHg for 4 hours, using a 0.5 μm filter. Then, filtration under reduced pressure was performed to obtain a water-based ink for inkjet recording.
[0111]
The microcapsules in the obtained water-based ink have an average particle size of 0.09 μm, exhibit stable dispersion over a long period without aggregates, and printing using a thermal jet ink jet printer is stable. The obtained printed matter showed high blackness without bleeding. The obtained printed matter was not disturbed in characters and the printing density was high.
[0112]
(Example 2)
20 parts of carbon black and 20 parts of styrene-acrylic acid-methacrylic acid resin (styrene / acrylic acid / methacrylic acid = 77/10/13; molecular weight 50,000 / acid value 160), 210 parts of water, 35 parts of glycerin, It put into the mixed solution of 8 parts of triethanolamine, 90 parts of methyl ethyl ketone, and 40 parts of isopropyl alcohol, and it stirred at room temperature for 4 hours using the dispersion stirrer, and obtained the preliminary dispersion liquid.
[0113]
Prepare a spike mill manufactured by Inoue Seisakusho using zirconia beads with a diameter of 0.3 mm as dispersion media. Place the pre-dispersed liquid obtained above in the supply and recovery tank and cool the tank and the entire pipe to 5 ° C. Then, the pressure was reduced to 30 mmHg and continuous dispersion was performed for 8 hours to obtain a black colored resin particle dispersion containing pigment microcapsules as the pigment dispersion. In dispersing the pigment, the apparatus was configured as shown in FIG.
[0114]
While stirring under reduced pressure at 30 mmHg to the resulting black dispersion, a mixed solution of 30 parts of glycerin and 210 parts of water was added dropwise at a rate of 5 ml / min, and then methyl ethyl ketone and isopropyl alcohol were distilled off using a rotary evaporator. Concentration was performed to obtain a final black colored resin particle dispersion having a carbon black content of 8%.
[0115]
To 100 parts of the resulting aqueous dispersion, 20 parts of glycerin, 5 parts of propylene glycol propyl ether and 75 parts of water were added, stirred at 30 mmHg for 4 hours, filtered under reduced pressure using a 0.5 μm filter, and water-based for inkjet recording Ink was used.
[0116]
The microcapsules in the obtained water-based ink have an average particle size of 0.09 μm, show stable dispersion over a long period without agglomerates, and continuous printing using a piezoelectric inkjet printer is stable. The obtained printed matter showed no blackness and high blackness, and was excellent in water and light resistance.
[0117]
【The invention's effect】
The pigment dispersion obtained by the pigment dispersion method using the dispersion apparatus of the present invention and the colored resin particle dispersion obtained by the colored resin particle production method have a fine particle size, extremely excellent dispersion stability, and are water-based for inkjet recording. When applied to ink, it has excellent dispersion stability and enables stable inkjet ejection characteristics and excellent print quality.
[Brief description of the drawings]
FIG. 1 is a media mill having a decompression structure in which a supply tank and a recovery tank of the present invention are the same.
FIG. 2 is a media mill having a pressure reducing structure in which the pressure of the recovery tank becomes negative with respect to the pressure of the supply tank of the present invention.
[Explanation of symbols]
1A Dispersing device A
1B Dispersing device B
2 Vessel wall
3 Rotor
4 tanks
5 Ultrasonic oscillator
6 Degassing mouth
7 pipes
8 Pressure control valve
9 Switching valve

Claims (10)

少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含み,固体顔料が液媒体に安定分散するまで,当該容器と分散機構との間に,当該混合物を連続的に循環させる機構を設け、前記減圧可能な容器として、固体顔料と液媒体との混合物を供給する供給容器,及び固体顔料が液媒体に安定分散した顔料分散液を回収する回収容器を別々に両方有し、すくなくともいずれか一方から減圧を行い、供給容器の圧力に対して,回収容器の圧力が負圧になるようにしたことを特徴とするメジアミルからなる顔料分散装置。It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. was, and a Mejiamiru dispersing the solid pigment in a liquid medium until the solid pigment is stably dispersed in a liquid medium, between the container and the dispersing mechanism, a mechanism for circulating the mixture continuously, the vacuum Possible containers include a supply container that supplies a mixture of a solid pigment and a liquid medium, and a recovery container that collects a pigment dispersion in which the solid pigment is stably dispersed in the liquid medium, and the pressure is reduced from at least one of them. A pigment dispersing apparatus comprising a media mill , wherein the recovery container pressure is negative relative to the supply container pressure . 固体顔料と液媒体との混合物が通過する,運動するメジア群を含む前記分散機構が,ベッセルの内壁に微小間隙を介して,外壁を有する回転可能なロータを有し,その微小間隙にメジアが運動可能となる様に充填されており,ロータを回転させるとともに,固体顔料と液媒体との混合物を,分散機構中で略栓流となる様にして通過させる請求項1記載の顔料分散装置。  The dispersion mechanism including a moving media group through which a mixture of a solid pigment and a liquid medium passes has a rotatable rotor having an outer wall through a minute gap on the inner wall of the vessel, and the media is located in the minute gap. 2. The pigment dispersion apparatus according to claim 1, wherein the pigment dispersion apparatus is filled so as to be movable, rotates the rotor, and allows the mixture of the solid pigment and the liquid medium to pass through the dispersion mechanism in a substantially plug flow. 固体顔料と液媒体との混合物を略栓流とするために,ロータ表面に,メジアに回転と衝撃力を与える突起と,当該混合物の流れ方向とは逆方向にメジアが戻される様に溝を形成した請求項2記載の顔料分散装置。  In order to make the mixture of the solid pigment and the liquid medium substantially plug flow, a protrusion is provided on the rotor surface that gives rotation and impact force to the media and a groove so that the media is returned in the direction opposite to the flow direction of the mixture. The pigment dispersion apparatus according to claim 2 formed. 容器の一部に超音波発信機構を設けた請求項1〜記載の顔料分散装置。Pigment dispersing apparatus according to claim 1 to 3, wherein the part provided with the ultrasonic wave transmission mechanism of the container. 分散液を冷却可能なように,少なくとも装置の一部が冷却構造を設けた請求項1〜記載の顔料分散装置。The dispersion so as to be cooled, at least the pigment dispersion according to claim 1-4, wherein a portion of which is provided a cooling structure of the apparatus. 少なくとも減圧可能な構造を有する容器と,固体顔料と液媒体との混合物を運動するメジア群間を通過させ分散させる分散機構を有する,固体顔料の液媒体への分散が行われる部分を減圧可能とした,固体顔料を液媒体に分散させるメジアミルとを含む顔料分散装置を用いて,固体顔料を液媒体に安定分散させるに当たり,当該混合物を循環させて,減圧下で,固体顔料を液媒体に安定分散させ、前記減圧可能な容器として、固体顔料と液媒体との混合物を供給する供給容器,及び固体顔料が液媒体に安定分散した顔料分散液を回収する回収容器を別々に両方有し、すくなくともいずれか一方から減圧を行い、供給容器の圧力に対して,回収容器の圧力が負圧になるようにすることを特徴とする顔料分散方法。It is possible to depressurize the part where the solid pigment is dispersed in the liquid medium, having at least a container having a structure capable of depressurization and a dispersion mechanism for passing and dispersing the mixture of the solid pigment and the liquid medium through the moving media group. In order to stably disperse the solid pigment in the liquid medium by using a pigment dispersion apparatus containing mediamyl which disperses the solid pigment in the liquid medium, the mixture is circulated and the solid pigment is stabilized in the liquid medium under reduced pressure. As a container that can be dispersed and depressurized, it has both a supply container that supplies a mixture of a solid pigment and a liquid medium, and a recovery container that collects a pigment dispersion in which the solid pigment is stably dispersed in the liquid medium. A pigment dispersion method, wherein pressure is reduced from any one of the two so that the pressure in the recovery container becomes negative relative to the pressure in the supply container . 液媒体として,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体を用いる請求項記載の顔料分散方法。The pigment dispersion method according to claim 6 , wherein a liquid medium containing at least a resin having an acid value, water, and a base is used as the liquid medium. 液媒体として,少なくとも,酸価を有する樹脂と,水と,塩基を含む液媒体を用い,前記樹脂に対する貧溶媒を加えて,液媒体中の固体顔料を前記樹脂で被覆して,固体顔料の微粒子表面を被覆して液媒体に安定分散させる請求項記載の顔料分散方法。A liquid medium containing at least a resin having an acid value, water, and a base is added as a liquid medium, a poor solvent for the resin is added, and the solid pigment in the liquid medium is coated with the resin, so that the solid pigment The pigment dispersion method according to claim 6, wherein the fine particle surface is coated and stably dispersed in a liquid medium. 液媒体が,酸価を有する樹脂と,水と,樹脂溶解可能な水溶性有機溶剤と,塩基からなり,かつ,樹脂に対する貧溶媒が,水または樹脂を溶解しない水溶性有機溶剤である請求項または記載の顔料分散方法。The liquid medium comprises a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, and a base, and the poor solvent for the resin is a water-soluble organic solvent that does not dissolve water or the resin. The pigment dispersion method according to 7 or 8 . 液媒体が,酸価を有する樹脂と,水と,樹脂溶解可能な水溶性有機溶剤と,塩基からなり,かつ,水または樹脂を溶解しない水溶性有機溶剤の水溶液からなる前記樹脂に対する貧溶媒を加えて,液媒体中の固体顔料を前記樹脂で被覆して,固体顔料を被覆して液媒体に安定分散させた後に,少なくとも樹脂溶解可能な水溶性有機溶剤を液媒体から除去する請求項または記載の顔料分散方法。A poor solvent for the resin, wherein the liquid medium is composed of a resin having an acid value, water, a water-soluble organic solvent capable of dissolving the resin, a base, and an aqueous solution of water or a water-soluble organic solvent that does not dissolve the resin. in addition, by coating the solid pigment in a liquid medium in the resin, after stabilize dispersed in a liquid medium by coating the solid pigment claim 7 to be removed from the liquid medium at least a resin dissolvable water-soluble organic solvent Or the pigment dispersion method of 8 .
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