Page 267 - Materials Chemistry, Second Edition
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250       Practical Design Calculations for Groundwater and Soil Remediation



               (d)  Assuming the packing material only occupies a small fraction
                   of the total reactor volume, the hydraulic retention time can be
                   estimated by:
                   hydraulic residence time = (V/Q) = (Ah)/Q
                       = (47.2 ft )(3 ft) ÷ [20 gpm/(1 ft /7.48 gal)] = 53 min
                                                 3
                              2
              Discussion:
              It is relatively difficult for the effluent of a bioreactor to meet the dis-
                charge limit in the ppb level. Activated-carbon adsorbers may be
                needed as a polisher to treat the effluent of the bioreactor before
                discharge.






           6.6  In Situ Groundwater Remediation

           6.6.1  Description of the In Situ Bioremediation Process
           Biological in situ treatment of organic COCs in aquifers is usually accom-
           plished by enhancing activities of indigenous subsurface microorgan-
           isms. Most of the in situ bioremediation is practiced in the aerobic mode.
           The microbial activities are enhanced by addition of inorganic nutri-
           ents and oxygen into the groundwater plume. The typical process con-
           sists of withdrawal of groundwater, addition of oxygen and nutrients,
           and reinjection of the enriched groundwater through injection wells or
           infiltration galleries. In addition to extraction of groundwater, addition
           of oxygen-releasing compounds (ORCs) to the plume can also be used
           instead.



           6.6.2  Addition of Oxygen to Enhance Biodegradation
           Groundwater naturally contains low levels of dissolved oxygen (DO).
           Even if it  is fully saturated with  air, the saturated dissolved oxygen
           (DO ) concentration in groundwater would only be in the neighborhood
               sat
           of 9 mg/L at 20°C. Biodegradation of organic COCs in the plume may
           need much more oxygen than those dissolved-oxygen molecules present
           in groundwater.
             Addition of oxygen to the groundwater can be done by air sparging or
           pure oxygen sparging. The oxygen in the injected air can raise the DO to its
           saturation level of 8 to 10 mg/L. With pure oxygen injection, the DO con-
           centrations of up to 40 to 50 mg/L can be achieved. DO level in the water
           can also be raised by addition of chemicals such as hydrogen peroxide and
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