Page 578 - Industrial Wastewater Treatment, Recycling and Reuse
P. 578

548   Index


          Cavitation coupled with Fenton      colloidal form and charged species
            description, 176–177                 pollutants, 87
            efficiency, 177                   cost, 130–131, 132–133
          Cavitation coupled with H 2 O 2 , 167–169  description, 526
          Cavitation coupled with ozone       dissociation, neutralization and
            advantages, 169–170                  association mechanism, 88–90
            combined process, schematic, 171f  dye wastewater treatment, 93–96
            limitations, 169–170              electrical double-layer suppression, 88–90
            ozone dosage optimization, 170–171  electro-coagulation and cavigulation,
          Cavitation coupled with photocatalyst  92–93
            batch reactors, schemes, 173f     flocculants and coagulants, 86–87
            combinatorial effects of UV and HC,  and flocculation, 86
                schemes, 174f                 hybrid materials, 91–92
            continuous reactors, schemes, 173f  Jar test apparatus, 90, 90f
            higher synergistic effect, 172–175  organic polymers, 92
            reduced efficiency problem, 171–172  PAC, commercial variations, 91–92
            UV and cavitation, 171–172        phenolic compounds removal, 324–325
          Cavitation inception number, 151–152  pollutants removal, wastewater
          CETPs. See Common effluent treatment   treatment, 86
                plants (CETPs)                positive/negative charges, 87
          CFD. See Computational fluid dynamics  surface charge and charge density, 87–88
                (CFD)                         types, 88, 89t
          Chemical and pharmaceutical production.  Coagulation/flocculation
                See Biological treatment      charge neutralization, 29
          Chemical manufacturing industrial   description, 28
                wastewater                    inorganic and organic, 28, 29
            COD range, 388                  Collaboration and joint research
            wastewater compositions, 387, 388t   programs, 534
          Chemical oxidation, phenolic compounds  Command Area Development (CAD)
                removal, 325–326                 Program, 315
          Chemical oxygen demand (COD)      Common effluent treatment plants (CETPs)
            average concentration, 423        advantages, 513
            biogas generation, 422–423        in chemical industries, 195
            bioreactor, 418–419               combined effluent treatment, industries,524
            concentration, 415, 423–424       feed effluent, 513
            cross-flow microfiltration, 411   industries, 524
            feed, bioreactor and permeate, 423–424  low-pressure steam, 513
            and OLR, 421                    Computational fluid dynamics (CFD)
            removal efficiencies, 409–411, 425f  applications, 68, 69
            stream AnMBR, 431                 improved clarifier designed, 68, 69f
            synthetic feed solution, 416      low-level gradually enlarged inlet, 69
            synthetic wastewater, 419         performance enhancement, 68, 69
            and TOC removal performance,      water treatment, recycling and reuse
                423–424                          applications, 68
          Coagulation                       Condensate process
            advantages and disadvantages, 92  boiler water, 440
            charge modification/neutralization,  cooling tower, 440
                86–87                         sugar shot, 439–440
   573   574   575   576   577   578   579   580   581   582   583