Kinetics of degradation of hydrocarbons in the contaminated soil layer.

This work presents kinetic parameters of the removal of hydrocarbons in the course of bioremediation of the soil contaminated with crude and oil derivatives, with special emphasis paid to polycyclic aromatic hydrocarbons. Bioremediation was carried out on a laboratory scale, with continuous and discontinuous recirculation of water through the soil column inoculated with the adapted bacterial population. Biodegradation of hydrocarbons can be described by the following equation--ln C = ln C0- kt--which is most often used in the literature to describe degradation of hydrocarbons, and by the equation--ln C = ln C0- kt0.5--which is determined on the basis of experimental data (except for pyrene and chrysene, for which a linear equation was used). A comparison of the two models showed a significant difference in the calculated remediation times, indicating that it is not realistic to expect a simple kinetic model to provide precise and accurate descriptions of concentrations during different seasons and in different environments. The results indicated that once contaminated with hydrocarbons, soil can be slowly brought to the previous state provided that no new contamination has occurred.

Formation of by-products in the course of intermediate ozonation of groundwater pretreated with ozone and polyaluminium chloride.

Formation of aldehydes and trihalomethanes during intermediate ozonation of water pretreated with ozone and polyaluminium-chloride was monitored in a pilot-scale study to optimize the drinking water treatment technology. The raw water was the groundwater, rich in natural organic matter, originated from the territory of the Northern Banat region in Vojvodina Province, Serbia and Montenegro. Monitoring of the parameters that have to meet prescribed criteria (permanganate value, TOC and THMFP removal) could not give an indication on how to split the required ozone dose between preozonation and intermediate ozonation. As the effects obtained regarding THMFP and TOC removal were similar, monitoring of aldehydes was performed, and this clearly showed that preozonation should be carried out with a dose > or = 0.4 mg O3/mg TOC to obtain the water with the smallest contents of aldehydes and the lowest specific content of glyoxal in the GAC filter influent.