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IbD PU Deliverable 3.1 Figure 47. Particle size distribution of the pharmaceutical compound produced in a DIJ mixer with different inlet jet velocities: 15 m/s (green), 10 m/s (red), 2.5 m/s (blue), and 1.1 m/s (pink) (Jiang et al., 2015). Notice that for the lower velocities, the CSDs are bimodal. 5.4 Mixer-settlers Mixer-settlers are widely used due to their reliability, operating flexibility, and high capacity. They can handle hard-to-disperse systems e.g. those with high interfacial tension and/or large phase density difference. They can also handle highly viscous liquids and solid-liquid slurries. A mixer-settler ordinarily consisted of two components: a mixer for contact of the two liquid phases to bring about the mass transfer and a settler for mechanical separation. Both components can be integral or separate. The operation can be in continuous or batch mode (Figure 48). Industrial deployment could be either in single stage or in cascaded mode. Outotec mixer-settler VSF® technology (Figure 49) was developed for hydrometallurgical processes with minimal mixing energy and pumping function, ensuring gentle, uniform mixing, and minimal crud formation. It has been designed to run at minimum operating costs, ensuring high profitability even during times of copper price fluctuations (Outotec, 2016). 47PDF Image | Solids handling for intensified process technology
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