Page 220 - Vogel's TEXTBOOK OF QUANTITATIVE CHEMICAL ANALYSIS
P. 220

7   ION EXCHANCE
             manner  to that  indicated  for cations.  In  dilute  solution multicharged
             anions are generally absorbed preferentially.
          (d)  When  a  cation  in  solution is  being  exchanged  for  an ion  of  different
             charge the relative affinity of the ion of higher charge increases in direct
             proportion to the dilution. Thus to exchange an ion of higher charge on
             the  exchanger  for  one  of  lower  charge in  solution, exchange  will  be
             favoured by increasing the concentration, while if  the ion of lower charge
             is in the exchanger and the ion of higher charge is in solution, exchange
             will be favoured by  high dilutions.
       2.  Nature of  ion exchange resin. The absorption* of ions will depend upon the
          nature  of  the functional  groups in  the  resin. It  will  also  depend  upon  the
          degree  of  cross-linking:  as  the  degree  of  cross-linking  is  increased,  resins
          become more selective towards ions of different sizes (the volume of the ion
          is  assumed  to  include  the  water  of  hydration);  the  ion  with  the  smaller
          hydrated  volume  will  usually be absorbed preferentially.

       Exchange of  organic  ions.  Although  similar principles  apply to  the exchange
       of organic ions, the following features must  also be taken into consideration.
       1.  The sizes of organic ions differ to a much greater extent than is the case for
          inorganic ions and may exceed  100-fold or even  1000-fold the average size
          of inorganic ions.
       2.  Many  organic  compounds  are  only  slightly  soluble  in  water  so  that
          non-aqueous ion exchange has an important role in operations with organic
           substance^.^'
          Clearly the application of macroreticular (macroporous) ion exchange resins
       will be often advantageous in the separation of organic species.
       Ion exchange capacity.  The total ion exchange capacity of a resin is dependent
       upon the total number of ion-active groups per unit weight of material, and the
       greater  the  number  of  ions,  the  greater  will  be  the  capacity.  The  total  ion
       exchange capacity is  usually  expressed  as millimoles  per  gram  of  exchanger.
       The  capacities  of  the  weakly  acidic  and  weakly  basic  ion  exchangers  are
       functions of  pH, the former reaching moderately constant values at pH above
       about  9 and  the  latter at  pH  below  about  5.  Values  for  the  total  exchange
       capacities,  expressed  as  mm01 g-'  of  dry  resin,  for  a  few  typical  resins  are:
       Duolite C225 (Na'  form), 4.5-5;  Zerolit 226 (H'  form), 9-10;  Duolite A113
       (Cl- form), 4.0; Amberlite IR-45, 5.0. The total exchange capacity expressed as
       mm01 ml - ' of  the wet  resin is about 3 - 3 of  the mm01 g - ' of  the dry resin.
       These figures are useful in estimating very approximately the quantity of  resin
       required  in a determination: an adequate excess must  be  employed, since the
       'break-through'  capacity is often much less than the total capacity of the resin.
       In most cases a  100 per cent excess is satisfactory.
          The exchange capacity of  a cation exchange  resin may be measured  in the
       laboratory by determining the number of milligram moles of sodium ion which
       are absorbed by 1 g of the dry resin in the hydrogen form. Similarly, the exchange
       capacity of a strongly basic anion exchange resin is evaluated by measuring the
       amount of chloride ion taken up by  1 g of dry resin in the hydroxide form.

        *The term absorption is used whenever ions or other solutes are taken up by an ion exchanger. It
        does not imply any specific types of forces responsible for this uptake.
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