Page 390 - Industrial Wastewater Treatment, Recycling and Reuse
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362   Industrial Wastewater Treatment, Recycling, and Reuse


          obtained for 4-NP, 4-CP, and phenol, respectively. The maximum desorp-
          tion was higher for AES-loaded adsorbents among the activated groups,
          reaching 32.53%, 39.55%, and 58.01% for 4-NP, 4-CP, and phenol. For
          4-NP, HNO 3 is a better desorbing agent, while for 4-CP and phenol,
          NaOH was found to be a good desorbing agent. The study indicates that
          4-NP desorption is the most difficult among 4-NP, 4-CP, and phenol.


          8.9 DISPOSAL AND COST ANALYSIS

          The safe disposal of phenol-loaded adsorbents is an environmental problem
          because leaching of the loaded adsorbents due to rain or percolated water
          may occur. Some of the methods, with their own inherent advantages
          and limitations, include elution, incineration, and pyrolysis. In the elution
          method, there is both recovery of the adsorbate molecules and regeneration
          of the adsorbent for subsequent use in a number of cycles. Although simple
          and inexpensive, there is some loss in efficiency after three or four cycles of
          desorption that may be due to blocking of the pores present on the adsorbent
          surface. The phenol-loaded adsorbent can be incinerated at high tempera-
          tures to yield ash, which can be recycled and reused appropriately. The
          release of toxic gases is one of the major disadvantages associated with
          the incineration process, especially in the case of chlorinated phenols. This
          method of regeneration involves a high cost of energy. However, a lot of
          research is required to make the adsorption method technoeconomically
          feasible.
             Cost is an important parameter for comparing adsorbent materials. It is
          usually the cost of the adsorbent that determines the cost of the adsorption
          process. The capacity/dose of the adsorbent and kinetics control the cost
          of treatment. The total cost for the preparation of the adsorbent can be cal-
          culated in a stepwise manner where the breakup costs of heating, drying,
          chemicals, and other overhead expenses are taken into consideration. The
          typical cost of special-grade AC materials is generally above Rs. 1000 per kg
          and many times runs into several thousand rupees per kg. The costs of the
          adsorbents used in the present study are less than Rs. 700 per kg.

          8.10 Summary
          The adsorption technique, especially using new adsorbent materials, in
          wastewater treatment provides a promising alternative to treat industrial
          wastewaters, in general, and phenolic industrial effluents, in particular.
          The study on several activated/nonactivated biomass-derived adsorbents
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