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112   Industrial Wastewater Treatment, Recycling, and Reuse


          of wastewater treatment. The separation of lactic acid/lactate salt can be
          accomplished mainly using solvent extraction, ion exchange, adsorption,
          distillation, and membrane separation (Scholler et al., 1993; Aljundi et al.,
          2005; Schlosser et al., 2005; Lee and Kim, 2011). Joglekar et al. (2006) have
          recently reviewed these different methods for the removal of lactic acid and
          have confirmed that the uptake of lactic acid for sorption by Dowex
          MWA-1 is much higher than that for extraction by Alamine 336. The main
          limitation of the method of solvent extraction is in the form of the toxicity of
          the solvent, especially with respect to microorganisms apart from solvent
          losses due to miscibility of the two phases and operating problems. Adsorp-
          tion studies using silicalite molecular sieves were reported recently by
          Aljundi et al. (2005). However, their capacities were very low—of the order
          of 55 g/kg adsorbent as compared to the typical capacity of 210 g/kg in the
          ion exchange resin Amberlite IRA-35. Sorption capacity with commercial
          polymeric adsorbents such as XAD-4, XAD-7, and XAD-16 are very much
          lower—with/without modification, although sorption capacity can be sig-
          nificantly altered with surface modification (Figure 2.11). A high sorption
          capacity of  360 g/kg can be obtained using carbon-based/modified car-
          bon adsorbents. With ion exchange, the sorption capacity for weak base
          ion exchange resins is also high—  360 g/kg on Dowex MWA-1
          (Figure 2.12). Thus, from many materials in the adsorbent and ion exchange
          resin class, the ion exchange resin appears to be most suitable for acid





               2.4
                   Lactic acid on polymeric     Lactic acid on polymeric
               2.0  adsorbents (NaOH treated)  2  adsorbents (NH  treated)
                                                        3
              Acid adsorbed, meq/g  1.6  XAD-4  Acid adsorbed, meq/g  1  XAD-4
                     XAD-7
                     XAD-16
                                                    XAD-16
                                                    XAD-7
               1.2
               0.8

               0.4

               0.0                           0
                 0.0  0.2  0.4  0.6  0.8  1.0  0.0  0.2  0.4  0.6  0.8  1.0  1.2  1.4
                Equilibrium acid concentration, meq/cc  Equilibrium acid concentration, meq/cc
          Figure 2.11 Adsorption of lactic acid on polymeric adsorbent with surface modification
          (Bhandari et al., 2006).
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