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Sepsci*11*TSK*Venkatachala=BG
                                                                                  I / CENTRIFUGATION  21


           rotor and are useful for comparing sedimentation  term,  . In Stokes’ equation, the term 6  r describes
           times for different rotors. The k-factor is derived  the frictional coefTcient, f 0 , for a spherical par-
           from the equation:                              ticle. The correction term,  , is calculated as the ratio
                                                           of the frictional resistance, f, encountered by a par-
                                             2
                                    13
                k"ln (r max !r min ) 10 /(3600  )          ticle of nonspherical geometry to that encountered by
                                                           a sphere of the same volume, or:
                            11
                 "2.53 10  ln (r max !r min )/rpm 2  [18]
                                                                           "f /f 0 "f /6  r          [22]
           where r max and r min are the maximum and minimum
           distances from the centrifugal axis, respectively.  The equation describing the terminal velocity for
             Eqn [18] shows that the lower the k-factor, the  nonspherical particles in a centrifugal Reld may be
           shorter the time required for pelleting. If the sedi-  rewritten as:
           mentation coefRcient of a particle is known, then        dx/dt"[d e (  P !  M )  x]/18    [23]
                                                                                        2
                                                                             2
           the rotor k-factor can also be calculated from the
           relation:                                       where d e is the diameter of a sphere whose volume
                                                           equals that of the sedimenting particle (d e /2 is the
                               k"TS                  [19]  Stokes radius).
                                                             The net result of this modiRcation is that non-
           where T is the time in hours required for pelleting  spherical particles are predicted to sediment more
           and S is the sedimentation coefRcient in Svedberg  slowly, which is a more accurate depiction of their
           units.                                          real-world behaviour.
             When k is known (normally provided by the manu-  In addition to deviations from spherical-particle
           facturer), then eqn [19] may be rearranged to calcu-  geometry, there are other effects that can lead to
           late the minimum run time required for particle  departure from predicted behaviour (nonideality)
           pelleting.                                      during sedimentation. For example, many biological
             For runs conducted at less than the maximum rated  particles interact with the medium via hydration, the
           rotor speed, the k-factor may be adjusted according  extreme case being for those particles with osmotic
           to:                                             properties, which can result in drastic changes in
                                                           particle density and, in turn, sedimentation coef-
                        k adj "k(rpm max /rpm act ) 2  [20]  Rcients. Interparticle attractions, e.g. charge or hy-
                                                           drophobic  effects,  may  increase  the  effective
           where rpm max and rpm act are the maximum rated  viscosity of the medium. In more severe cases such
           rotor speed and actual run speed, respectively.  attractions can lead to poor separations where the
             k-Factors are also useful when switching from a ro-  centrifugal energy is insufRcient to disrupt the
           tor with a known pelleting time, t 1 , to a second rotor  attractions between particles that are targeted for
           of differing geometry by solving for t 2 in the  separation. This latter effect is aggravated by the
           relation:                                       fact that the larger or denser particle will lead as the
                                                           particle pair migrates toward the rotor wall while
                                                     [21]  the smaller or lighter attached particle follows in its
                             t 1 /t 2 "k 1 /k 2
                                                           wake, and therefore experiences less frictional drag.
           where t 1 , t 2 , k 1 and k 2 are the pelleting times and  Particles may also concentrate locally to increase the
           k-factors for rotors 1 and 2, respectively.     effective medium density, or form aggregates
                                                           that yield complicated sedimentation patterns. Be-
           Deviation from Ideal Behaviour                  cause of such deviations from ideal behaviour, equiv-
                                                           alent sedimentation coefRcients, SH,deRned as
           Eqns [13] and [14] showed the relative impact on
                                                           the sedimentation coefRcient of an ideal spherical
           settling velocity of the more important and control-
           lable experimental parameters. However, there are  particle, are often reported for a given set of experi-
           other effects that are more difRcult to char-   mental conditions.
           acterize and which can result in signiRcant deviations
           from the settling velocities predicted by these equa-  Filtration
           tions. The most common of these effects occurs  A mathematical description of liquid drainage from
           when the particles are nonspherical, as these equa-  a packed bed by centrifugal forces is essentially the
           tions are derived from Stokes’ equation assuming  same as that used to describe more conventional
           spherical  particles.  For  nonspherical  particles,  gravity or differential-pressure Rltration, the pri-
           eqns [13] and [14] may be modiRed with a correction  mary differences being that the centrifugal force
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