Page 254 - Materials Chemistry, Second Edition
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Groundwater Remediation                                          237



           6.3.3.4  COC Removal Rate by the Activated-Carbon Adsorber
           The removal rate by an activated-carbon adsorber (R removal ) can be calculated
           by using the following formula:

                                          = C(      ) Q                   (6.13)
                                    R removal  in  − C out
           In practical applications, the effluent concentration (C ) is kept below the
                                                            out
           discharge limit, which is often very low. Therefore, for a factor of safety, the
           term of C  can be deleted from Equation (6.13) in design. The mass removal
                    out
           rate is then essentially the same as the mass loading rate (R loading ):

                                  R removal ≅ R loading =  ( CQ)          (6.14)
                                                    in

           6.3.3.5  Change-Out (or Regeneration) Frequency
           Once the activated carbon reaches its capacity, it should be regenerated or
           disposed of. The time interval between two consecutive regenerations or the
           expected service life of a fresh batch of activated carbon can be estimated by
           dividing the capacity of the activated carbon in the adsorber with the COC
           removal rate (R removal ) as:


                                        T =  M removal                    (6.15)
                                            R removal


           6.3.3.6  Configuration of the Activated-Carbon Adsorbers
           If multiple activated-carbon adsorbers are used, the adsorbers are often
           arranged in series and/or in parallel. If two adsorbers are arranged in series,
           a monitoring point should be located at the effluent of the first adsorber. A
           high effluent concentration from the first adsorber indicates that this adsorber
           is reaching its capacity. The first adsorber is then taken off-line and the sec-
           ond adsorber is shifted to be the first adsorber. Consequently, the capacity of
           both adsorbers would be fully utilized, and the compliance requirements are
           met. If there are two parallel streams of adsorbers, one stream can always be
           taken off-line for regeneration or maintenance, and the continuous operation
           of the process will not be interrupted.
             The following procedure can be used to complete the design of an acti-
           vated-carbon adsorption system:

              Step 1:  Determine the design adsorption capacity as described previ-
                    ously (also see Example 6.9).
              Step 2:  Determine the required volume of the activated-carbon adsorber
                    by using Equation (6.10).
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