A method for the determination of power consumption of industrial agitators in non-Newtonian fluids on the basis of measurements on a model device is presented. The applicability of this method for purely viscous, time dependent and viscoelastic fluids is discussed. The method was tested experimenta
Scale-up of power consumption in agitated ball mills
✍ Scribed by Herbert Weit; Jörg Schwedes
- Publisher
- John Wiley and Sons
- Year
- 1987
- Tongue
- English
- Weight
- 534 KB
- Volume
- 10
- Category
- Article
- ISSN
- 0930-7516
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✦ Synopsis
P l O I bar1 total pressure References tCMs [m3,,/m3cMsh] CMS factor volume of hydrogen produced per unit time and unit adsorber volume mercury-, apparent density [ I ] Lohmuller, R.,
📜 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
AH = enthalpy change, cal./g.-mole psoz = partial pressure of sulfur dioxide, atm. poa = partial pressure of oxygen, atm. R = universal gas constant, 1.98 cal./(g.-mole) ( O K . ) ro = initial reaction rate, 1b.-moles sulfur dioxide/ (hr.) AS = entropy change, cal./ (g.-mole) ( O K . ) T = absolute