By Hendrikus Egidius Antonia van den Akker; J J Derksen
Normally, fluid blending and the similar multiphase contacting procedures have continuously been considered as an empirical know-how. Many facets of combining, dispersing and contacting have been relating to strength draw, yet figuring out of the phenomena was once constrained or qualitative on the such a lot. particularly over the past decade, even if, plant operation goals have tightened and product necessities became stricter. the general public expertise as to safeguard and environmental hygiene has elevated. The force in the direction of greater levels of sustainability within the approach industries has recommended for reduce quantities of solvents and for larger yields and better selectivities in chemical reactors. All this has ended in a
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Extra info for 10th European Conference on Mixing: proceedings of the 10th European conference, Delft, the Netherlands, July 2-5, 2000
This is shown in Figures 4a - c. It must be noted that the vortex of the hydrofoil impeller could not be visualised completely since measurements within the impeller swept region were not possible. From Figure 4 the total extent of the trailing vortices generated behind each stirrer blade of each impeller type can be determined. Some details of the trailing vortices are summarised in table 1, which contains the total length, the diameter, the radial (from outer tip), axial (from lower tip) and tangential (from ~ = 0 ~ extents of the vortices.
Chem. , 74 (1996) 3. 3. M. C. R. Bush, 1988,. 2nd Int. Conf. Bioreactor Fluid Dynamics, R. , 37. 4. S. Ruszkowski, 8th Eur. Conf. E. Syrup. Series 136 (1994) 283. 5. W. Nienow, Chem. Eng. , 52 (1997) 2557. 6. H. Fruman, P. Cerrutti, T. Pichon and P. Dupont, J Fluids Engng, 117 (1995), 162. 7. R. J. L. Billet, J Fluids Engng, 113 (1991) 496. 8. K. F. Reeder, A. S. Dickey, Recents Progres en Genie des Procedes, 11 (1997) 115. 9. K. van't Riet, W. Bruijn W. M. Smith, Chem. Eng. , 31 (1976) 407. 10.
In this paper, the point at which fully developed turbulence in the impeller region does not penetrate throughout the bulk of the tank is examined for a D=T/3 pitched blade turbine (PBT) at C=T/3 and C=T/6. U c x. A _ - Lc . U c v (1) Fully developed turbulence occurs when the inertial forces in the system are so large that the viscous forces become negligible and the accurate definition of this point is critically dependent on appropriate choice of the characteristic length (Lc) and velocity (Uc) scales.
10th European Conference on Mixing: proceedings of the 10th European conference, Delft, the Netherlands, July 2-5, 2000 by Hendrikus Egidius Antonia van den Akker; J J Derksen