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    Flotation kinetics shown in Figure 35.30 with 5 and 10 W of acoustic power applied also show an excellent performance. It should be noted that the acoustic powers used to vary the flotation kinetics have been quite low and could clearly be expanded. Figure 35.25. Schematic of Denver cell conditioned for ultrasonic-assisted flotation. Figure 35.26. Acoustic field in the medium

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    Conventional flotation cells allow a small amount of clay slimes to be recovered with the water that reports to the froth product. A column cell Fig. 19) virtually eliminates this problem by washing the clay slimes from the froth using a countercurrent flow of wash water. This feature allows columns to produce higher quality concentrate coals at the same coal recovery. Figure 19. Illustration

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    The separation performance achieved by each cell approached and, in some cases, exceeded the ultimate performance predicted by release analysis. A comparison of the test results indicates differences in the selectivity obtained by each flotation column on the basis of both ash and sulfur rejection. This finding may be due to variations in cell hydrodynamics and the ability to support a deep

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