By R.Q. Honaker, W.R. Forrest
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It is evident that there is excellent agreement between the results from the two fluidization methods in both Figures 4A and 4B indicating that the final result is independent of whether the particles are sized and then fluidized, or fluidized and then sized. Further, the cumulative yield versus density plot indicates excellent agreement between the sink-float method and the two fluidization methods. There is, however, an obvious discrepancy between the cumulative yield versus cumulative ash results, with the sink-float method producing the higher yield at a given ash.
2003 by the Society for Mining, Metallurgy, and Exploration. All rights reserved. Electronic edition published 2009. MODELING OF HINDERED-SETTLING COLUMN SEPARATIONS Feed Solids Feed Water Overflow Particles Water Teeter Water Teeter Water Distributor Pressure Sensor Pneumatically Actuated Control Valve Underflow FIGURE 1 Schematic of the hindered-settling column The solids are fed through the top opening of the column along with feed water. The function of the feed water is to prevent the solids from bridging in the feed tube, thereby ensuring a constant flow of feed solids into the column.
Electronic edition published 2009. HINDERED SETTLING IN LIQUID FLUIDIZED BEDS Overflow (Product) Product Plates Feed Reject Plates Fluidization Water Distributor Plate Underflow (Rejects) A schematic representation of the Reflux Classifier, consisting of a fluidized bed housing and two sets of parallel inclined plates FIGURE 7 typically 15 t/h, which represents a loading more than three times higher than for a conventional system (Honaker and Mondal, 1999). Additional results from a typical separation of a coal and mineral matter feed are shown in Figure 8 using a set of partition curves.
Advances in gravity concentration by R.Q. Honaker, W.R. Forrest