Abstract
The white rot fungus Phanerochaete chrysosporium was utilized for the degradation of a model chlorinated organic compound, i.e., 2-chlorophenol, using three different reactor configurations: a batch fermenter, a chemostatic reactor with the fungus immobilized on a silica-based porous biocatalyst support, and a packed-bed reactor where the fungus was immobilized on balsa wood particles. A comparison of the effectiveness of these reactor configurations was made by determining the overall first-order kinetic rate constant for the degradation process for each one of the reactors. The packed-bed reactor proved to be the most effective configuration examined in this study because of the low shear and the presence of a solid support. Therefore, this type of reactor was studied in greater detail. In the packed-bed reactor oxygen was supplied by either sparged air or hydrogen peroxide additions. The degradation process was followed by taking samples from five different ports mounted alongside the packed-bed column. Glucose, nitrogen, 2-chlorophenol, chloride ion, and ligninolytic enzyme concentrations were measured in each sample. In this reactor the fungus was able to mineralize 2-chlorophenol in concentrations up to 500 ppm. About 80% to 94% of the chlorine initially present in the 2- chlorophenol fed to the system was recovered as chloride ion.
Original language | English (US) |
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Pages (from-to) | 213-229 |
Number of pages | 17 |
Journal | Hazardous Waste and Hazardous Materials |
Volume | 9 |
Issue number | 3 |
DOIs | |
State | Published - 1992 |
All Science Journal Classification (ASJC) codes
- Toxicology
- Waste Management and Disposal
- Pollution