Microhydrodynamic analysis of nanogrinding in stirred media mills
β Scribed by D. Eskin; O. Zhupanska; R. Hamey; B. Moudgil; B. Scarlett
- Publisher
- American Institute of Chemical Engineers
- Year
- 2005
- Tongue
- English
- Weight
- 178 KB
- Volume
- 51
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
The dynamics of the milling media in a turbulent flow is considered. The mean velocity of the milling beads is calculated on the assumption that the power spent on stirring is transferred into the energy of turbulent eddies. The energy spent on stirring dissipates as a result of mediaβliquid viscous friction, lubrication, and by inelastic collisions of the beads with each other. The maximum force at which the milling beads can compress particles between them is calculated by the Hertzian theory of elastic impact. The frequency of compressions for a single particle is evaluated by probabilistic analysis. A criterion of milling efficiency, based on calculating the energy spent on the plastic particle deformation, is proposed. A numerical study of the milling bead dynamics and their interactions with the particles in the mixing tank is performed. The numerical results are in qualitative agreement with the experimental data. Both the numerical and experimental analyses show that, from the perspective of hydrodynamics, an optimization of stirred media mills can be achieved by choosing the optimum size and concentration of the milling media. Β© 2005 American Institute of Chemical Engineers AIChE J, 2005
π SIMILAR VOLUMES
The physical model to describe comminution and dispersion processes is based on the idea that the comminution result is determined by the number of stress events, SN, and the stress intensity, SI. Thus, comminution behaviour of a mill is characterized by the frequency of stress events, SF, and the s
## Abstract Gas/liquid mass transfer has been investigated in an aerated stirred tank using nonβNewtonian media and carbon dioxide as absorbent and gas phase respectively. The volumetric mass transfer coefficients at different operational variables have been measured. The nonβNewtonian media (liqui