Page 44 - Introduction to Colloid and Surface Chemistry
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Kinetic properties  35

        where x\  and x 2  are  the  distances  of  the  boundary  from  the  axis of
        rotation  at  times  t\  and t 2.  Therefore,


                                                               (2.18)


        It is evident from the above expressions that the appropriate  diffusion
        coefficient  must also be measured  in order  that  molecular or  particle
        masses may be determined  from sedimentation  velocity  data. In  this
        respect,  a  separate  experiment  is  required,  since  the  diffusion
        coefficient  cannot  be determined accurately in situ, because there  is a
        certain  self-sharpening  of  the  peak  due  to  the  sedimentation
        coefficient  increasing  with  decreasing  concentration.
          Care  must be taken  to ensure that the  system under investigation
        remains uncoagulated. This applies to any technique for determining
        molecular or particle  masses.  s, D and v are  corrected  to a  standard
        temperature,  usually  20°C,  and  should  be  extrapolated  to  zero
        concentration.
          With  polydispersed  systems  either  a  broadening of  the  boundary
        (in  addition  to that  caused  by diffusion)  or  the  formation of distinct
        peaks  representing  the  various fractions is observed. Sedimentation
        does  not  provide  an  unequivocal  method  for  establishing  the
        homogeneity  of a colloidal system.  For example,  a mixture of serum
        albumin and haemoglobin is homogeneous  with respect  to sedimenta-
        tion  velocity but  the  two proteins  are  easily distinguished from  each
        other  by  electrophoresis.
          Knowledge of M  and  v enables D 0 and, hence, the  ratio D^/D  (the
        f fictional  ratio)  to  be calculated.


        Sedimentation  equilibrium

        Consider  the  flow  of  molecules  or  particles  across  an  area  A  in  a
        colloidal solution where the concentration  is c and the  concentration
        gradient is dc/dx . The  rate of flow is cA  (dx/dt)  due  to  sedimentation,
        and,  from  Pick's  first  law,  -DA  (dc/djc)  due  to  diffusion.  When
        sedimentation equilibrium  is attained,  the  net flow is zero,  so that

              dx    dc
             c—  = D —
              d?    dx
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