Page 194 - Materials Chemistry, Second Edition
P. 194

Vadose Zone Soil Remediation                                     177



              •  Dry bulk density of soil, ρ b
              •  Total bulk density of soil, ρ t


           Example 5.16:   Estimate the Cleanup Time (in the
                         Presence of Free-Product Phase)

           Recently, a gasoline spill occurred at a gasoline station and caused subsur-
           face contamination. A soil-venting well (4-in. diameter) was installed at a
           site. The pressure in the extraction well is 0.9 atm, and the radius of influence
           of this soil-venting well has been determined to be 50 ft.
             Estimate the required cleanup time for total petroleum hydrocarbon (TPH)
           using the following information:

              •  Permeability of the formation = 1 darcy
              •  Well screen length = 20 ft
              •  Viscosity of air = 0.018 centipoise
              •  Temperature of the formation = 20°C
              •  Porosity = 0.35
              •  Organic content in soil = 0.01
              •  Degree of water saturation = 40%
              •  Dry bulk density of soil = 1.6 g/cm 3
              •  Total bulk density of soil = 1.8 g/cm 3
              •  Size of the plume = 6,500 ft 3
              •  Initial average TPH concentration in soil = 6,000 mg/L
              •  Required cleanup level = 100 mg/L
              •  Overall efficiency factor relative to theoretical removal rate = 0.11



              Solution:
               (a)  The flow rate has been determined in Example 5.10 to be 0.216
                   m /min, or 7.6 ft /min.
                     3
                                  3
              Presence of the Free-Product Phase
               (b)  Determine  the  maximum  possible  TPH  concentration  in  soil
                   absent  of  free  product,  X   (use the procedure  illustrated in
                                           sat
                   Example 5.3):
                   Since no Henry’s constant and K  data are available for gasoline,
                                                ow
                       we use those of toluene, one of the common gasoline compo-
                       nents, as an approximation:
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