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TECHNICAL PAPERS

Ceramic Micro/Nanoparticle Size Evolution in Wet Grinding in Stirred Ball Mill

[+] Author and Article Information
Jiann-Cherng Su, Steven Y. Liang

George W. Woodruff School of Mechanical Engineering, Georgia Institute of Technology, Atlanta, GA

Wang Lin Liu, Tzu Chi Jan

Precision Machinery Research and Development Center, Taichung, Taiwan, ROC

J. Manuf. Sci. Eng 126(4), 779-786 (Feb 04, 2005) (8 pages) doi:10.1115/1.1811117 History: Received January 28, 2004; Revised July 21, 2004; Online February 04, 2005
Copyright © 2004 by ASME
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References

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Gao,  M., and Forssberg,  E., 1995, “Prediction of Product Size Distributions for a Stirred Ball Mill,” Powder Technol., 84, pp. 101–106.
Frances,  C., and Laguerie,  C., 1998. “Fine Wet Grinding of an Alumina Hydrate in a Ball Mill,” Powder Technol., 99, pp. 147–153.
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Spicer,  P. T., and Pratsinis,  S. E., 1996, “Coagulation and Fragmentation: Universal Steady-State Particle-Size Distribution,” AIChE J., 42(6), pp. 1612–1620.
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Spicer,  P. T., and Pratsinis,  S. E., 1996, “Shear-Induced Flocculation: The Evolution of Floc Structure and the Shape of the Size Distribution at Steady State,” Water Res., 30(5), pp. 1049–1056.
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Barthelemes,  G., Pratsinis,  S. E., and Buggisch,  H., 2003, “Particle Size Distributions and Viscosity of Suspensions Undergoing Shear-Induced Coagulation and Fragmentation,” Chem. Eng. Sci., 58, pp. 2893–2902.
Saffman,  P., and Turner  J., 1956, “On the Collision of Drops in Turbulent Clouds,” J. Fluid Mech., 1(1), pp. 16–30.
Holland, F. A., and Chapman, F. S, 1966, Liquid Mixing and Processing in Stirred Tanks, Reinhold, London.
Kapur,  P. C., 1972, “Self-Preserving Size Spectra of Comminuted Particles,” Chem. Eng. Sci., 27(2), pp. 425–431.
http://www.ceramics.nist.gov/srd/summary/TiO2.htm (bending 3-pt)
http://environmentalchemistry.com/yogi/periodic/Ti.html
Malvern Instruments Zetasizer 3000HS: Principles of Operation

Figures

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Ball milling chamber diagram
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Rotating cylinder diagram
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Rotating plate above stationary plate
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Fully coalesced aggregate
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(a) Coagulation of particles in section i with (a) smaller particles and (b) loss of particles of section i with same-sized particles
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Maximum particle diameter versus time, varying initial diameter (nm)
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Maximum particle diameter versus time, varying surface creation energy (J/m2)
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Maximum particle diameter versus time, varying viscosity (Pa-s)
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Maximum particle diameter versus time, varying speed (rpm)
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Maximum particle diameter versus time varying concentration
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Particle size distribution (ω=1200 rpm)
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Particle size distribution (ω=1800 rpm)
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Particle size distribution (ω=2400 rpm)
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Experiment particle size distribution measurements
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Experiment results of particle diameter versus time

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