Page 28 - Subyek Encyclopedia - Encyclopedia of Separation Science
P. 28

Sepsci*11*TSK*Venkatachala=BG
                                                                                  I / CENTRIFUGATION  23


             The types of separation to be discussed focus on the  to separating particles of similar density according
           separation of solids from liquid media using any of  to size (classiRcation), an approximate order of mag-
           the recovery modes described above. Discussion of  nitude difference in mass between the particles is
           simpler batch-mode operation is emphasized for sim-  needed for differential sedimentation to be effective.
           plicity. Three primary types of centrifugal separations  The main disadvantage of separating a homogenate
           are discussed: differential sedimentation, density  in batch mode is that the centrifugal Reld required to
           gradient and Rltration, with density gradient being  pellet the larger or denser particles that are initially
           further divided into rate-zonal and isopycnic (in  nearer the axis of rotation is capable of pelleting
           isopycnic separations, particles sediment until they  smaller or lighter particles initially closer to the outer
           attain a position in the gradient at which the medium  wall (Figure 3). Product purity or recovery may be
           density is equal to their own).                 improved by either recentrifuging the supernatant to
                                                           obtain more pellet, or by resuspending the pellet and
                                                           recentrifuging to obtain higher purity. When purity
           Differential Sedimentation
                                                           is the primary concern, this approach can still be
           As previously shown by the equations describing sedi-  used as a preparatory step to provide an enriched
           mentation (eqns [13] and [14]), larger and/or denser  fraction for subsequent puriRcation. However,
           particles will sediment more rapidly in a centrifugal  a more efRcient one-step approach is to layer the
           force Reld and will thus pellet onto the outer wall of  sample mixture on top of the preloaded medium.
           the rotor faster than smaller or lighter particles. Most  Stopping the run before the lighter or smaller con-
           applications are based on this difference in be-  taminant particles reach the rotor wall allows them to
           haviour, referred to as differential sedimentation  be decanted with the supernatant. An alternative is
           or pelleting. In a simple batch-mode pelleting separ-  to use a continuous-feed rotor in which the sample
           ation, a sample mixture called the homogenate (im-  mixture is introduced near the axis of rotation and
           miscible liquids or solid suspensions) is placed into  the supernatant, containing the smaller or lighter
           a centrifuge container or rotor, and separated into  unsedimented particles, is continuously discharged.
           two fractions as depicted in Figure 3. The un-  A more efRcient approach is to layer or feed the
           sedimented material is termed the supernatant and  sample to the top of a preloaded density gradient (see
           the sedimented material is the pellet. This approach  below).
           works well when the objective is to pellet all the solid
           particles or to clarify the liquid. Such separations are  Density Gradient Centrifugation (DGC)
           also commonly used in the laboratory for ‘quick and
           dirty’ separations or where the objective is to enrich  DGC, developed in the 1950s, also relies on dif-
           or clarify materials for subsequent analysis.   ferential sedimentation behaviour to separate sample
             Obtaining high purity separations by differen-  components, but compensates for some of the disad-
           tial sedimentation is more difRcult. With respect  vantages of homogeneous media and also allows for
                                                           the simultaneous separation of multicomponent mix-
                                                           tures. This is accomplished by the use of a density
                                                           gradient, i.e. a liquid medium that increases in density
                                                           from the layers nearest the axis of rotation to those
                                                           farthest away. As will be discussed, this is achieved
                                                           through variation in the concentration of an aqueous
                                                           solute, or other gradient material, across the rotor.
                                                           With minimal precautions, density gradients are sur-
                                                           prisingly stable for extended periods, even with the
                                                           rotor stopped. DGC separations are more extensively
                                                           used for smaller-scale research applications in con-
                                                           trast to large-scale pelleting separations that are more
                                                           common to industrial applications. DGC may be con-
                                                           ducted as either rate or isopycnic separations.


                                                           Rate-zonal separations This technique, also called
                                                           classiRcation, is used to separate particles of similar
                                                           density according to size. For batch separations, the
           Figure 3 Differential sedimentation or pelleting. (Courtesy of  sample mixture is layered on top of a preloaded
           Beckman Instruments, Inc.)                      medium, as shown in Figure 4. During a rate-zonal
   23   24   25   26   27   28   29   30   31   32   33