Page 475 -
P. 475

ACTIVATED CARBON PROCESSES              14.23


                                                         Effluent
                    Influent

                                                 :' i'i..- ~).:
                                                  •  .:.~..-
                                                  .:~  !. i
                                                 ?. ~:.!i"2.:
                                                  .   .   ..   •   .
                                                 " .'.-'...:2  .."
                                                  •  .....
                                                 .   ..."'".   ..
                                     Effluent

                       Downflow in series
                                                 Influent
                                                Pulsed bed
                    Influent                             Effluent

                                                           r








                                                    T      t
                                      D
                                 Effluent   Influent
                      Downflow in parallel   Upflow-expanded in series
                  FIGURE 14.12  Commonly used GAC contactor configurations.




        TABLE  14.5  Guide to Selection of GAC  System Configuration
          Adsorption system
            configuration                     Applicable if:
        Single adsorber    Low carbon exhaustion rate (usage rate) occurs.
        Fixed beds in series   High carbon exhaustion rate occurs. High effluent quality must be
                           ensured at all times.
        Fixed beds in parallel
                           High system pressure drop is minimized. Large total flow rate is
                           required.
        Moving beds, upflow
                           High carbon exhaustion rate occurs. High effluent quality is required.
                           Either some carbon fines can be tolerated in the effluent, or carbon
                           adsorption is followed by filtration.
        Expanded beds, upflow   High suspended solids are present in the influent, and some suspended
                           solids can be tolerated in the effluent.
   470   471   472   473   474   475   476   477   478   479   480