Page 390 - Academic Press Encyclopedia of Physical Science and Technology 3rd Chemical Engineering
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              Membranes, Synthetic, Applications                                                          325

              reasons.  The  first  relates  to  critical  applications—e.g.,
              medical/immunological separations and salt removal from
              solutions of genetically engineered proteins—where leak-
              age of undesirable species from the feed stream into the
              permeate cannot be tolerated. (Also see Sections VI and
              VII.) The second aspect is the absence of concentration
              polarization arising from convective flow through an ul-
              trafilter, for example, and the consequent accumulation of
              rejected species in the boundary layer.


                2.  Donnan Dialysis
              Ion exchange membranes contain high concentrations of
              fixed  charges.  They  are  permeable  to  ions  of  opposite
              charge (counterions) but repel ions of the same charge
              (coions). Protons are the only exception; they can perme-
              atefreelythroughhydrationpassagesinananionexchange
              membrane. The functions of anion- and cation-exchange
                                                                FIGURE 39  Donnan dialysis application to the separation of sul-
              membranes are illustrated in Fig. 38.
                                                                furic acid from aluminum sulfate. Al 2 (SO 4 ) 3  designated by   ❡ and
                Donnan dialysis functions through the interaction be-
                                                                H 2 SO 4  by   (HPD, Inc.).
              tween ions and ion-exchange membranes in the absence
              of  an  externally  applied  electrical  field.  When  an  ion
                                                                the ion exchange membrane into a water stream, form-
              exchange membrane separates two electrolyte solutions,
                                                                ing sulfuric acid. Aluminum cations are rejected by the
              and a second electrolyte with the same counterion but a
                                                                fixed positive charges on the membrane and exit as a less
              nonpermeating coion is added to one side of the mem-
                                                                acidic aluminum sulfate stream for recovery or disposal.
              brane, counterions migrate across the membrane until the
                                                                Similar applications include the recovery of sulfuric acid
              charge separation stops further flow and electroneutrality
                                                                from nickel sulfate steel pickling waste, and the recovery
              is established on both sides of the membrane. This phe-
                                                                of nitric and hydrofluoric acids produced during stainless
              nomenon is known as Donnan equilibrium. Donnan dialy-
                                                                steel etching. Donnan dialysis is effective because high
              sis refers to the process of separating ionic components in
                                                                concentration gradients yield concentrated products, and
              a feed stream according to their tendency to migrate across
                                                                because direct input of electrical energy is not required to
              ion-exchange membranes to achieve equilibrium.
                                                                achieve separation.
                The example shown in Fig. 39 illustrates the treatment
              of an aluminum anodizing bath waste stream by Donnan
              dialysis. Sulfate ions and protons freely permeate from a  3.  Electrodialysis
              feed stream of aluminum sulfate and sulfuric acid across
                                                                Although the development of electrodialysis desalination
                                                                technology  predated  that  of  reverse  osmosis  (q.v.),  at
                                                                present both processes compete favorably with distillation
                                                                for potable water production. In electrodialysis, salts are
                                                                removed from a feed solution by using an electric current
                                                                (DC) to transport ions across anion-exchange and cation-
                                                                exchange membrane pairs. By restricting the migration
                                                                of ions to no more than one adjacent solution compart-
                                                                ment, as shown in Fig. 40(a), alternate streams become
                                                                enriched and depleted of electrolytes. Electrodialysis op-
                                                                erates most economically when the feed water contains
                                                                less than 0.5% TDS, but medium-salinity seawaters (up
                                                                to about 1.2% TDS) can also be desalted. Product wa-
                                                                ter containing less than 0.01% TDS can be obtained. The
              FIGURE  38  Selective  diffusion  across  ion-exchange  mem-
              branes.  (a)  Anion  exchange,  and  (b)  cation  exchange.  Metal  capability of electrodialysis to remove salts from neutral
              cations are designated by M , anion A , proton H , and the fixed  solutes is also exploited in other applications, e.g., desalt-
                                 +
                                                +
                                        −
              charges in the membrane by + and −.               ing proteins.
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