Page 136 - Industrial Wastewater Treatment, Recycling and Reuse
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110   Industrial Wastewater Treatment, Recycling, and Reuse


          Table 2.3 Some examples of industrial wastewater streams
          Industry            Acids          Composition     Reference

          Pulping process     Formic, acetic  4–10%          Othmer (1958)
          Synthetic fatty acid  Formic, acetic,  5, 5, 2.5, & 2%  Matsarenko et al.
                                propionic,     respectively    (1969)
                                butyric
          Industrial effluents  Formic, acetic,  0.5–5%      Helsel (1977)
                                propionic
          Manufacture of      Formic, acetic,  <10%          Parulekar et al.
            formic, acetic      oxalic                         (1982); Ricker
            acids                                              et al. (1980);
            Oxidation of                                       Wadekar and
            organics e.g.,                                     Sharma
            p-xylene,                                          (1981b);
            cyclohexane                                        Kawabata et al.
                                                               (1981)
          Dyes and pigment    Sulfuric,      <1%             –
            industry            phthalic,
            Acid leached        oleic
            wastewater
          Electroplating      Hydrochloric,  High, up to 10%  Bonev and
            industry            sulfuric                       Nenov (2006)




          to 4%, depending upon the source of generation. Removal of acids from
          aqueous streams containing low to medium concentrations of acids—
          organic, inorganic, or both—is an important problem in chemical proces-
          sing industries, necessitating selection of suitable separation methodologies
          on the basis of the composition of the stream. Ion exchange, adsorption, sol-
          vent extraction, membrane separation, reactive distillation, reactive extrac-
          tion, membrane-based solvent extraction, and emulsion liquid membrane
          (ELM) separation are considered as promising separation methods for devis-
          ing suitable strategies. Ion exchange resins, in general, and weak base resins,
          in particular, are most commonly employed for lower concentrations.
          Because large volumes that contain low concentrations of acids need to
          be treated, ion exchange is the most convenient method of treatment in
          many cases. The primary goal in such cases is largely removal of acids from
          the solution, not separation. However, acid separation is important in acid
          manufacturing units where another acid is usually obtained as a by-product,
          for example, formic acid from the manufacture of acetic acid. Thus, the
          selection of an ion exchange resin for any particular application, whether
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