Fig. 1. Map showing the most contaminated area, where trichloroethylene (TCE) concentrations in the soil were >10 mg kg1. Lines C and E are tomography lines (Fig. 3).
Fig. 4. Simulated two-dimensional spreading of the NAPL phase in a vertical cross section during a hypothetical spill of trichloroethylene (TCE). The color contours in the figure represent NAPL saturation.
Fig. 5. The simulation model used for the pilot scale simulations. I6, I7, I12 and I13 are injection wells; E8-E11 (vertical) and H1-H5 (horizontal) are extraction wells.
Fig. 7. Simulation results showing steam break through the clay layer around Injection Wells I6 and I7. The gray area (around Wells I6 and I7) has temperatures exceeding 60°C. The color contours represent trichloroethylene (TCE) concentrations in the water.
Fig. 8. Simulation results showing the effects of the newly installed Injection Wells I12 and I13. The gray area (around Well I13) has temperatures exceeding 60°C. The color contours represent trichloroethylene (TCE) concentrations in the water.
Fig. 9. Planned full-scale remediation system and simulated temperature distribution along the lower edge of the clay layer after 2 wk of cyclical-rotational steaming from Wells I12 through I15. In these simulations the former Injection Well I7 was used for vapor extraction.
Fig. 10. Proportion of trichloroethylene (TCE) (%) extracted with in the simulations by cyclical steam injection (S1) and rotational steam injection (S2).