Page 39 - Subyek Encyclopedia - Encyclopedia of Separation Science
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34   I / CENTRIFUGATION/ Derivatization



















































           Figure 10 Major industrial applications for continuous centrifuges. (Courtesy of Alfa Laval Separations.)



           ports at different radial distances as dictated by  Solids-ejecting stacked-disc centrifuges (Figure 11B)
           the relative concentration of the liquids. Commercial  are more suitable for processing samples with solids
           units are available with liquid throughput capacities  contents to about 15% by volume. These units oper-
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           of 60 m h  and holding capacities of 30 L. A vari-  ate similarly to the solids-retaining design, only solids
           ation on the solids-retaining disc centrifuge is the  or sludge that accumulate on the bowl wall are inter-
           cylindrical-bowl design shown in Figure 12, which  mittently discharged through a hydraulically ac-
           incorporates a series of concentric cylindrical re-  tivated, peripheral opening. Laboratory models to
           tainers for processing liquid}solid mixtures. Unlike  18 cm diameter and industrial units to 60 cm are
           the disc centrifuge, in which the feed stream is split  available, with the latter capable of throughputs in
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           and makes a single pass through the disc stack, in the  excess of 100 m h  . Applications for these units
           cylindrical-bowl design the liquid stream is routed  include catalyst recovery, clariRcation of paints and
           through each chamber in succession, resulting in  varnishes, treatment of radioactive waste water, and
           a longer residence time, more efRcient recovery,  copper extraction.
           and generally greater capacity (to 70 L). Applications  Continuous solids-discharge disc centrifuges, also
           of solids-retaining centrifuges of the stacked-disc or  called nozzle bowl separators (Figure 11C), are used
           cylindrical-bowl design include separation of cream  to process samples with solids contents ranging from
           from milk, organic waste from water, puriRcation of  5 to 30% by volume. In this design, solids are con-
           lubricating oils, or removal of water and solids from  tinuously discharged via backward-facing oriRces, i.e.
           jet fuel.                                       nozzles, closely spaced around the outer periphery of
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