JP2020015893A5 - - Google Patents

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JP2020015893A5
JP2020015893A5 JP2019069851A JP2019069851A JP2020015893A5 JP 2020015893 A5 JP2020015893 A5 JP 2020015893A5 JP 2019069851 A JP2019069851 A JP 2019069851A JP 2019069851 A JP2019069851 A JP 2019069851A JP 2020015893 A5 JP2020015893 A5 JP 2020015893A5
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pigment dispersion
aqueous pigment
producing
range
aqueous
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JP2019069851A
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JP2020015893A (en
JP6863399B2 (en
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Claims (8)

混練装置が備える容器に、少なくとも顔料と樹脂とを供給する工程[1]、前記容器の内容物(a1)を、25℃での動的粘弾性測定によって求められる角周波数1rad/sにおける貯蔵弾性率が200kPa〜30000kPaの範囲内になるまで混練する工程[2]、前記工程[2]で得られた顔料混練物と、水性媒体とを混合する工程[3]、及び、前記工程[3]で得られた水性顔料分散体を、円筒型遠心分離装置を用い30℃〜70℃の範囲内で遠心分離処理する工程[4]を含む水性顔料分散体の製造方法。 In the step of supplying at least the pigment and the resin to the container provided in the kneading device [1], the content (a1) of the container is stored elastic at an angular frequency of 1 rad / s determined by dynamic viscoelasticity measurement at 25 ° C. A step of kneading until the ratio is within the range of 200 kPa to 30,000 kPa [2] , a step of mixing the pigment kneaded product obtained in the step [2] with an aqueous medium [3], and the step [3]. A method for producing an aqueous pigment dispersion, which comprises a step [4] of centrifuging the aqueous pigment dispersion obtained in (1) in the range of 30 ° C. to 70 ° C. using a cylindrical centrifuge device. 前記内容物(a1)の不揮発分が50質量%以上である請求項1に記載の水性顔料分散体の製造方法。 The method for producing an aqueous pigment dispersion according to claim 1, wherein the non-volatile content of the content (a1) is 50% by mass or more. 前記工程[2]は、前記内容物(a1)の温度を60℃〜120℃の範囲内に維持した状態で行う工程である請求項1または2に記載の水性顔料分散体の製造方法。 The method for producing an aqueous pigment dispersion according to claim 1 or 2, wherein the step [2] is a step performed in a state where the temperature of the content (a1) is maintained in the range of 60 ° C. to 120 ° C. 前記混練装置が閉鎖型混練装置である請求項1〜3のいずれか1項に記載の水性顔料分散体の製造方法。 The method for producing an aqueous pigment dispersion according to any one of claims 1 to 3, wherein the kneading device is a closed kneading device. 前記混練装置がプラネタリーミキサーである請求項4に記載の水性顔料分散体の製造方法。 The method for producing an aqueous pigment dispersion according to claim 4, wherein the kneading device is a planetary mixer. 前記工程[3]は、前記顔料混練物に対して前記水性媒体を供給することによって水性顔料分散体の不揮発分を10質量%〜30質量%の範囲に調整する工程である請求項1〜5のいずれか1項に記載の水性顔料分散体の製造方法。0091 The step [3] is a step of adjusting the non-volatile content of the aqueous pigment dispersion in the range of 10% by mass to 30% by mass by supplying the aqueous medium to the pigment kneaded product. The method for producing an aqueous pigment dispersion according to any one of the above. 0091 前記工程[4]は、前記工程[3]で得られた水性顔料分散体として25℃での粘度が13mPa・s以下の水性顔料分散体を用い、それを円筒型遠心分離装置で、遠心分離処理する工程である請求項6に記載の水性顔料分散体の製造方法。0098 In the step [4], an aqueous pigment dispersion having a viscosity of 13 mPa · s or less at 25 ° C. is used as the aqueous pigment dispersion obtained in the step [3], and the aqueous pigment dispersion is centrifuged by a cylindrical centrifuge. The method for producing an aqueous pigment dispersion according to claim 6, which is a step of treating. 0098 前記工程[4]は、前記円筒型遠心分離装置が備えるローターに、前記工程[3]で得られた前記水性顔料分散体を供給し、前記水性顔料分散体の温度を30℃〜70℃の範囲内に維持して遠心分離処理する工程であって、前記ローターの容積に対する前記工程[3]で得られた水性顔料分散体の供給量(体積)の比率[前記工程[3]で得られた水性顔料分散体の供給量(体積)/ローターの容積]×100が1000%〜8000%であり、かつ、前記円筒型遠心分離装置の遠心加速度が8000G〜20000Gの範囲である請求項7に記載の水性顔料分散体の製造方法。100−101 In the step [4], the aqueous pigment dispersion obtained in the step [3] is supplied to the rotor provided in the cylindrical centrifuge, and the temperature of the aqueous pigment dispersion is set to 30 ° C. to 70 ° C. It is a step of maintaining within the range and performing the centrifugation treatment, and the ratio of the supply amount (volume) of the aqueous pigment dispersion obtained in the step [3] to the volume of the rotor [obtained in the step [3]. The supply amount (volume) of the aqueous pigment dispersion / the volume of the rotor] × 100 is 1000% to 8000%, and the centrifugal acceleration of the cylindrical centrifuge is in the range of 8000G to 20000G. The method for producing an aqueous pigment dispersion according to the above. 100-101
JP2019069851A 2018-07-17 2019-04-01 Method for Producing Pigment Kneaded Product and Aqueous Pigment Dispersion Active JP6863399B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2018134122 2018-07-17
JP2018134122 2018-07-17

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JP2020015893A JP2020015893A (en) 2020-01-30
JP2020015893A5 true JP2020015893A5 (en) 2020-10-08
JP6863399B2 JP6863399B2 (en) 2021-04-21

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JP2022147738A (en) * 2021-03-23 2022-10-06 富士フイルムビジネスイノベーション株式会社 Manufacturing method of carrier for electrostatic charge image development, manufacturing method of electrostatic charge image developer, image formation method and carrier for electrostatic charge image development

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JP4534118B2 (en) * 2003-07-31 2010-09-01 Dic株式会社 Aqueous pigment dispersion and method for producing the same
JP4561053B2 (en) * 2003-08-13 2010-10-13 Dic株式会社 Kneaded product for aqueous pigment dispersion and method for producing aqueous pigment dispersion and ink composition using the same
JP2009062466A (en) * 2007-09-07 2009-03-26 Toyo Ink Mfg Co Ltd Method for preparing finely pulverized organic pigment
JP6075931B2 (en) * 2009-07-10 2017-02-08 Dic株式会社 Method for producing aqueous pigment dispersion
JP2012219144A (en) * 2011-04-06 2012-11-12 Dic Corp Method for producing aqueous pigment dispersion for inkjet recording, aqueous pigment dispersion for inkjet recording, and aqueous ink for inkjet recording
JP6136288B2 (en) * 2013-01-18 2017-05-31 Dic株式会社 Method for producing aqueous pigment dispersion and aqueous ink for inkjet recording
JP6705164B2 (en) * 2015-12-21 2020-06-03 Dic株式会社 Method for producing aqueous pigment dispersion

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