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Bioremediation 5 - 10 September 1993 <br /> Aerobic in-situ bioremediation of the subsurface saturated and unsaturated zones generally involves <br /> establishing a hydrostatic gradient through the area of contamination. For saturated zone <br /> remediation, typically, nutrients and oxygen are added to the contaminated areas by infiltration <br /> trenches, injection wells, or air sparging wells. Ground water flow is controlled and maintained by <br /> dowtngradient interceptor wells (recovery wells) or trenches. The extracted ground water can be <br /> further treated above-ground by activated carbon, aeration, bioremediation, etc. Finally the ground <br /> water is inoculated with oxygen and nutrients and reinjected. This continuous recirculation is <br /> carried on until the site has been cleaned up. Recovery of the percolating water and ensuring <br /> adequate distribution of oxygen are the most difficult aspects of this method. Hydraulic control of <br /> injection and recovery water must he achieved in order to ensure that hydrocarbons are not spread <br /> and are effectively recovered. The bioreclamation system must achieve an even distribution of <br /> water flow through the treatment area. <br /> Aerobic in-situ bioremediation of the unsaturated zone is affected by many factors, including <br /> dissolved oxygen levels, soil moisture content, soil permeability, soil porosity, oxidation-reduction <br /> potential, temperature, pH, compound availability and concentration, nutrient availability, and the <br /> natural microbial community, Oxygen and nutrients are added by infiltration trenches or injection <br /> wells with water table interceptor wells. Water and nutrients are injected and recirculated by <br /> extracting and reinjecting, as in ground water bioremediation. Aeration depends on the total amount <br /> of air filled pore space. Elimination of air-filled pore space by waterlogging or compaction reduces <br /> oxygen transfer. Many monitoring wells may be needed to determine the effectiveness of the <br /> system. Due to poor mixing with these types of systems it may be necessary to treat for a long time <br /> to ensure that pockets of contaminated soil ate treated. Soils containing silts or clays are not <br /> favorable for bioremediation due to their relative impermeabilities and adsorptive capacities. <br /> An alternative to recirculating water through the unsaturated zone involves manipulation of the soil <br /> air by adding oxygen, humidity, and gaseous nutrients by air irgection wells_ Soil gas flow is <br /> controlled with vacuum extraction wells. This method requires careful monitoring of soil moisture <br /> to prevent desiccation. <br /> For in-situ biodegradation, about 3 lbs of oxygen are required for every pound of petroleum <br /> hydrocarbons degraded. There are several methods to introduce oxygen to the suhtlrrFtce: <br /> 1, Sparging into the saturated zone (biosparging) can deliver about 4 ppm at the injection point; <br /> 2, Injection of air or oxygen into the vadose zone (bioventing) can deliver up to 10 ppm; <br /> 3. Hydrogen peroxide (FIzO2) can be dissolved and injected at above 500 ppm and will break <br /> down to oxygen and water during transport through the contaminated area AOI in high <br /> concentrations can be toxic to microbes); <br /> 4. Injection of aerated water; <br /> To operate in-situ bioremediation systems, extensive knowledge of the subsurface is required. <br /> Knowledge of soil characteristics is necessary to track hydrocarbon migration and adsorption onto <br /> soils. Hydraulic relationships between multiple aquifers is necessary to evaluate potential migration <br /> of hydrocarbons between aquifers. It is also necessary to understated the horizontal and vertical <br /> components and rate of flow of ground water and seasonal and daily water table fluctuations. <br /> OT ' d 800' nN £E=6 26' 9T daS ON I31 <br />