JP2013057899A5 - - Google Patents
Download PDFInfo
- Publication number
- JP2013057899A5 JP2013057899A5 JP2011197468A JP2011197468A JP2013057899A5 JP 2013057899 A5 JP2013057899 A5 JP 2013057899A5 JP 2011197468 A JP2011197468 A JP 2011197468A JP 2011197468 A JP2011197468 A JP 2011197468A JP 2013057899 A5 JP2013057899 A5 JP 2013057899A5
- Authority
- JP
- Japan
- Prior art keywords
- toner
- particle dispersion
- heating
- particles
- aggregated
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Description
請求項5に係る発明は、
前記熱交換処理において、前記第1配管における前記凝集粒子分散液の流通、及び前記第2配管における前記トナー粒子分散液の流通を、下記式(1)で示されるレイノルズ数Reが100以上15000以下を満たすように行う請求項3に記載の静電荷像現像用トナーの製造方法。
・式(1):Re=[配管相当直径(m)×分散液の流速(m/s)×分散液の流体密度(kg/m3)]/分散液の流体粘度(Pa・s)
The invention according to claim 5
In the heat exchange treatment, the flow of the aggregated particle dispersion in the first pipe and the flow of the toner particle dispersion in the second pipe have a Reynolds number Re represented by the following formula (1) of 100 to 15000. The method for producing a toner for developing an electrostatic image according to claim 3, wherein the toner is developed so as to satisfy
Formula (1): Re = [equivalent pipe diameter (m) × dispersion flow velocity (m / s) × dispersion fluid density (kg / m 3 )] / dispersion fluid viscosity (Pa · s)
請求項10に係る発明は、
前記熱交換器において、前記第1配管における前記凝集粒子分散液の流通、及び前記第2配管における前記トナー粒子分散液の流通を、下記式(1)で示されるレイノルズ数Reが100以上15000以下を満たすように行う請求項8に記載の静電荷像現像用トナーの製造装置。
・式(1):Re=[配管相当直径(m)×分散液の流速(m/s)×分散液の流体密度(kg/m3)]/分散液の流体粘度(Pa・s)
The invention according to claim 10 is:
In the heat exchanger, the flow of the aggregated particle dispersion in the first pipe and the flow of the toner particle dispersion in the second pipe have a Reynolds number Re represented by the following formula (1) of 100 to 15000. 9. The apparatus for producing a toner for developing an electrostatic charge image according to claim 8, wherein the toner is developed so as to satisfy the condition.
Formula (1): Re = [equivalent pipe diameter (m) × dispersion flow velocity (m / s) × dispersion fluid density (kg / m 3 )] / dispersion fluid viscosity (Pa · s)
Claims (10)
熱交換器により、加熱前の前記トナー粒子分散液と加熱後の前記トナー粒子分散液との間で熱交換処理を行い、加熱前の前記トナー粒子分散液の温度を上昇させ、加熱後の前記トナー粒子分散液の温度を降下させる工程と、
を有する静電荷像現像用トナーの製造方法。 Heating the toner particle dispersion in which the toner particles are dispersed, and controlling the shape of the toner particles;
Using a heat exchanger, heat exchange treatment is performed between the toner particle dispersion before heating and the toner particle dispersion after heating, the temperature of the toner particle dispersion before heating is increased, and the temperature after heating is increased. Reducing the temperature of the toner particle dispersion;
A method for producing a toner for developing an electrostatic charge image.
前記原料分散液中で、前記樹脂粒子を少なくとも凝集させ、凝集粒子を形成する工程と、
前記凝集粒子が分散された凝集粒子分散液を加熱して、前記凝集粒子を融合・合一し、トナー粒子を形成する工程と、
熱交換器により、加熱前の前記凝集粒子分散液と、前記トナー粒子が分散された加熱後のトナー粒子分散液と、の間で熱交換処理を行い、加熱前の前記凝集粒子分散液の温度を上昇させ、加熱後の前記トナー粒子分散液の温度を降下させる工程と、
を有する静電荷像現像用トナーの製造方法。 Preparing a raw material dispersion in which at least resin particles are dispersed;
A step of aggregating at least the resin particles in the raw material dispersion to form aggregated particles;
Heating the aggregated particle dispersion in which the aggregated particles are dispersed to fuse and coalesce the aggregated particles to form toner particles;
A heat exchanger performs a heat exchange treatment between the aggregated particle dispersion before heating and the heated toner particle dispersion in which the toner particles are dispersed, and the temperature of the aggregated particle dispersion before heating. And lowering the temperature of the toner particle dispersion after heating, and
A method for producing a toner for developing an electrostatic charge image.
・式(1):Re=[配管相当直径(m)×分散液の流速(m/s)×分散液の流体密度(kg/m3)]/分散液の流体粘度(Pa・s In the heat exchange treatment, the flow of the aggregated particle dispersion in the first pipe and the flow of the toner particle dispersion in the second pipe have a Reynolds number Re represented by the following formula (1) of 100 to 15000. The method for producing a toner for developing an electrostatic image according to claim 3, wherein the toner is developed so as to satisfy
Formula (1): Re = [pipe equivalent diameter (m) × dispersion flow velocity (m / s) × dispersion fluid density (kg / m 3 )] / dispersion fluid viscosity (Pa · s)
加熱前の前記トナー粒子分散液と加熱後の前記トナー粒子分散液との間で熱交換処理を行い、加熱前の前記トナー粒子分散液の温度を上昇させ、加熱後の前記トナー粒子分散液の温度を降下させる熱交換器と、
を有する静電荷像現像用トナーの製造方法。 Toner particle shape control means for heating the toner particle dispersion in which the toner particles are dispersed and controlling the shape of the toner particles;
A heat exchange treatment is performed between the toner particle dispersion before heating and the toner particle dispersion after heating, the temperature of the toner particle dispersion before heating is increased, and the toner particle dispersion after heating is heated. A heat exchanger that lowers the temperature;
A method for producing a toner for developing an electrostatic charge image.
前記凝集粒子が分散された凝集粒子分散液を加熱して、前記凝集粒子を融合・合一し、トナー粒子を形成するトナー粒子形成手段と、
加熱前の前記凝集粒子分散液と、前記トナー粒子が分散された加熱後のトナー粒子分散液と、の間で熱交換処理を行い、加熱前の前記凝集粒子分散液の温度を上昇させ、加熱後の前記トナー粒子分散液の温度を降下させる熱交換器と、
を有する静電荷像現像用トナーの製造装置。 Aggregated particle forming means for at least aggregating the resin particles in the raw material dispersion in which the resin particles are dispersed to form aggregated particles,
A toner particle forming means for heating the aggregated particle dispersion in which the aggregated particles are dispersed to fuse and coalesce the aggregated particles to form toner particles;
A heat exchange treatment is performed between the aggregated particle dispersion before heating and the heated toner particle dispersion in which the toner particles are dispersed, the temperature of the aggregated particle dispersion before heating is increased, and heating is performed. A heat exchanger for lowering the temperature of the toner particle dispersion later,
An apparatus for producing toner for developing an electrostatic charge image.
・式(1):Re=[配管相当直径(m)×分散液の流速(m/s)×分散液の流体密度(kg/m3)]/分散液の流体粘度(Pa・s) In the heat exchanger, the flow of the aggregated particle dispersion in the first pipe and the flow of the toner particle dispersion in the second pipe have a Reynolds number Re represented by the following formula (1) of 100 to 15000. 9. The apparatus for producing a toner for developing an electrostatic charge image according to claim 8, wherein the toner is developed so as to satisfy the condition.
Formula (1): Re = [equivalent pipe diameter (m) × dispersion flow velocity (m / s) × dispersion fluid density (kg / m 3 )] / dispersion fluid viscosity (Pa · s)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011197468A JP5831063B2 (en) | 2011-09-09 | 2011-09-09 | Method and apparatus for producing toner for developing electrostatic image |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011197468A JP5831063B2 (en) | 2011-09-09 | 2011-09-09 | Method and apparatus for producing toner for developing electrostatic image |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2013057899A JP2013057899A (en) | 2013-03-28 |
JP2013057899A5 true JP2013057899A5 (en) | 2014-11-13 |
JP5831063B2 JP5831063B2 (en) | 2015-12-09 |
Family
ID=48133811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2011197468A Expired - Fee Related JP5831063B2 (en) | 2011-09-09 | 2011-09-09 | Method and apparatus for producing toner for developing electrostatic image |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP5831063B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9182691B2 (en) * | 2013-10-18 | 2015-11-10 | Xerox Corporation | Continuous toner coalescence processes |
US9383666B1 (en) * | 2015-04-01 | 2016-07-05 | Xerox Corporation | Toner particles comprising both polyester and styrene acrylate polymers having a polyester shell |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000121284A (en) * | 1998-10-13 | 2000-04-28 | Osaka Gas Co Ltd | Heat transfer tube and heat conveying system |
JP4086039B2 (en) * | 2005-01-07 | 2008-05-14 | コニカミノルタビジネステクノロジーズ株式会社 | Toner manufacturing method and toner manufacturing apparatus |
US8080360B2 (en) * | 2005-07-22 | 2011-12-20 | Xerox Corporation | Toner preparation processes |
JP2007271238A (en) * | 2006-03-31 | 2007-10-18 | Kobelco & Materials Copper Tube Inc | Heat exchanger |
JP2008065247A (en) * | 2006-09-11 | 2008-03-21 | Mitsuru Nakano | Electrostatic charge image developing toner production device and electromotive non-return device |
JP2010100701A (en) * | 2008-10-22 | 2010-05-06 | Toray Ind Inc | Method for treatment of resin slurry |
-
2011
- 2011-09-09 JP JP2011197468A patent/JP5831063B2/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6147767B2 (en) | Heat exchanger suitable for carbon black production | |
JP2014191350A5 (en) | ||
JP2015004708A5 (en) | ||
JP2013020245A5 (en) | ||
CA2552190A1 (en) | Toner preparation processes | |
CN101118393A (en) | Method of manufacturing aggregated particles | |
JP2013057899A5 (en) | ||
CN103630327A (en) | Device for testing supercritical water fluidized bed two-phase flow and heat-transfer characteristic | |
RU2016109233A (en) | TONER PARTICLES CONTAINING COMPLEX POLYESTER AND STYROLACRYLATE POLYMERS, WITH A COMPOSITE POLYESTER Shell | |
TWI516443B (en) | Process for producing granular polysilicon | |
CN101968153A (en) | Liquid conveying and heating pipe | |
Eppinger et al. | Automated workflow for spatially resolved packed bed reactors with spherical and non-spherical particles | |
JP2013214065A5 (en) | Toner composition and method for producing the same | |
JP2013156591A5 (en) | ||
CN201978516U (en) | Heating chamber for bittern concentration and evaporation system | |
CN202328727U (en) | High-frequency fluid heater with new structure | |
CN108067167B (en) | Slurry bed reaction system and Fischer-Tropsch synthesis reaction method | |
CN201844744U (en) | Stirring device for heat exchange | |
US12013184B2 (en) | Device for producing expanded mineral granulated material | |
JP2014074905A5 (en) | Toner production method | |
CN203090909U (en) | Oil bath heating and cooling system | |
Cao et al. | Performance comparison of rod-baffle and segment-baffle heat exchangers using numerical simulations | |
CN103725863A (en) | Heating device of annular part and annular cavity of heating device | |
CN207891056U (en) | Collector for fume colloidal silica production | |
CN202018215U (en) | Double-pipe air heat exchanger |