Monday, 31 October 2005
143ab
In-Situ Biorestoration of Sediments Contaminated with Polycyclic Aromatic Hydrocarbons (Pahs)
Lei Wang, Department of Chemical & Materials Engineering, University of Cincinnati, 611 Rhodes Hall, Cincinnati, OH 45221, Rakesh Govind, Chemical Eng, University of Cincinnati, 611 Rhodes Hall, Cincinnati, OH 45221, and Henry Tabak, U.S. EPA, 26 W. Martin Luther King Drive, Cincinnati, OH 45268.
Restoration of contaminated sediments involves either mechanical removal of the sediment followed by treatment or in-situ treatment of the contaminants. Even after mechanical removal, considerable residues of the polluted material usually remain which require some form of in-situ treatment for eventual restoration. For in-situ treatment, conditions that appear to be rate determining are: (1) availability of oxygen; (2) availability of nutrients; and (3) nature of contaminants and sediment properties. There are significant variations in the redox potential of sediments as a function of depth. Aerobic bacterial biodegradation of PAHs is widely known and has been well studied. PAHs exhibit high octanol/water partition coefficient (KOW), which results in the accumulation of these compounds in fatty tissues with subsequent biomagnification in the food chain.
In this paper, a novel method of controlling the redox potential in contaminated sediments using semi-permeable synthetic membranes will be presented. The method allows in-situ biodegradation of PAHs in contaminated sediments while preventing the membranes from fouling. Experimental data will be presented on biodegradation rates of 18 PAHs ( 2 ring to 6 ring compounds) as a function of redox potential. The rate of biodegradation decreased with increasing ring size and decreasing oxidation potential. Experimental testing of the synthetic membranes showed that in-situ PAH degradation could be increased several fold by utilizing the membranes to increase the sediment oxidation potential. The membrane technology is widely applicable for in-situ biotreatment of contaminated freshwater and marine sediments. A detailed simulation model to estimate the required membrane area and treatment time will also be presented.
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