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Dynamic percolation extractor

Figure 14.10.3. Schematic of bench-scale dynamic percolation extractor. Figure 14.10.3. Schematic of bench-scale dynamic percolation extractor.
The sohd can be contacted with the solvent in a number of different ways but traditionally that part of the solvent retained by the sohd is referred to as the underflow or holdup, whereas the sohd-free solute-laden solvent separated from the sohd after extraction is called the overflow. The holdup of bound hquor plays a vital role in the estimation of separation performance. In practice both static and dynamic holdup are measured in a process study, other parameters of importance being the relationship of holdup to drainage time and percolation rate. The results of such studies permit conclusions to be drawn about the feasibihty of extraction by percolation, the holdup of different bed heights of material prepared for extraction, and the relationship between solute content of the hquor and holdup. If the percolation rate is very low (in the case of oilseeds a minimum percolation rate of 3 x 10 m/s is normally required), extraction by immersion may be more effective. Percolation rate measurements and the methods of utilizing the data have been reported (8,9) these indicate that the effect of solute concentration on holdup plays an important part in determining the solute concentration in the hquor leaving the extractor. [Pg.88]


See other pages where Dynamic percolation extractor is mentioned: [Pg.942]    [Pg.942]    [Pg.412]    [Pg.113]    [Pg.942]    [Pg.942]    [Pg.412]    [Pg.113]    [Pg.945]    [Pg.415]    [Pg.116]   
See also in sourсe #XX -- [ Pg.113 , Pg.117 ]




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