By Thaddeus J. Kowalski
Booklet by way of Kowalski, Thaddeus J.
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Extra resources for An Artificial Intelligence Approach to VLSI Design
Chiesa, V. Mathiesen, J. A. Melheim, B. Halvorsen, Numerical simulation of particulate flow by the Eulerian–Lagrangian and the Eulerian–Eulerian approach with application to a fluidized bed. Comput. Chem. Eng. 29 (2005) 291.  J. Sun, F. Battaglia, Hydrodynamic modeling of particle rotation for segregation in bubbling gas-fluidized beds, Chem. Eng. Sci. 61 (2006) 1470.  N. Xie, F. Battaglia, S. Pannala, Effects of using two-versus threedimensional computational modeling of fluidized beds Part I, hydrodynamics, Powder Technology 182 (2008).
These probes often give information about the Particle Size Distribution (PSD) and form, or the solution concentration, but do not allow estimating any physical characteristics of the suspension such as its apparent viscosity. This physicochemical parameter can be used to characterize and control a crystallization process. Very few on-line experimental techniques exist to directly determine the evolution of the apparent viscosity of a crystal slurry during a crystallization process. Moreover, very few theoretical or empirical correlations of the apparent viscosity of a suspension can be found in the literature.
Com, ISSN 1743-3533 (on-line) Computational Methods in Multiphase Flow V 41 from bubbly flow to other types of flow just after the singularity. The results are plotted on Baker’s map and are reported in Figure 19. However, since the departure from bubbly flow is decided on visual information, the transition criterion remains rather subjective and the results given in Figure 19 are only indicative. The second campaign of visualization is performed, using a high-speed camera, in a fully transparent setup that allows better optical access (without pressure taps).