Kinetics of the ozonation and aerobic biodegradation of wine vinasses in discontinuous and continuous processes.

The oxidation of the organic substrate present in wastewaters generated in wine distilleries ("wine vinasses") is studied by both an ozonation process and by an aerobic activated sludge system. The ozonation process is conducted in a subsequent first discontinuous and a second continuous periods. Values are reported of the organic matter removal, measured as chemical oxygen demand (COD) (5-25.2%) and as total aromatic compounds content (16.8-51.4%). The influences of the inlet ozone partial pressure, the hydraulic retention time in the reactor and the presence of UV radiation and H2O2 in addition to ozone are established. Approximate kinetic studies are conducted for both periods which lead to the evaluation of the apparent rate constants for the substrate decomposition 216l/(mol O3 h) and 232l/(g COD h), respectively. In the aerobic degradation by the activated sludge system, the evolution of the organic substrate and biomass are followed during both the discontinuous and continuous stages of the whole process, and COD removals from 31 to 85% are obtained for a hydraulic retention time between 24 and 72 h. For the first stage, a kinetic study is performed by using the Contois model, which applied to the experimental data provides the specific kinetic parameters: q(max)=0.190 g COD/(g volatile suspended solids (VSS)h) and K(1)=6.48g COD/g VSS. For the continuous period, the kinetic study carried out provides the specific rate constant for the substrate decomposition, q=0.027 g COD/(g VSS h).

[1]  S. Parekh,et al.  Fermentation of wood-derived acid hydrolysates in a batch bioreactor and in a continuous dynamic immobilized cell bioreactor by Pichia stipitis R , 1987 .

[2]  J. Charpentier,et al.  Mass-Transfer Rates in Gas-Liquid Absorbers and Reactors , 1981 .

[3]  D. Sales,et al.  A depurative process for wine distilleries wastes , 1987 .

[4]  F. Beltrán,et al.  Henry's law constant for the ozone-water system , 1989 .

[5]  David F. Ollis,et al.  Biochemical Engineering Fundamentals , 1976 .

[6]  R. S. Ramalho Introduction to Wastewater Treatment Processes , 1977 .

[7]  William H. Glaze,et al.  The Chemistry of Water Treatment Processes Involving Ozone, Hydrogen Peroxide and Ultraviolet Radiation , 1987 .

[8]  W H Glaze,et al.  Destruction of pollutants in water with ozone in combination with ultraviolet radiation. 3. Photolysis of aqueous ozone. , 1988, Environmental science & technology.

[9]  D. E. Contois Kinetics of bacterial growth: relationship between population density and specific growth rate of continuous cultures. , 1959, Journal of general microbiology.

[10]  C. Yao,et al.  Rate constants for direct reactions of ozone with several drinking water contaminants , 1991 .

[11]  B. Rindone,et al.  Ozone oxidation of compounds resistant to biological degradation , 1991 .

[12]  A. Evidente,et al.  Isolation, spectroscopy and selective phytotoxic effects of polyphenols from vegetable waste waters , 1992 .

[13]  J. Hoigne,et al.  Determination of ozone in water by the indigo method , 1981 .

[14]  M. Brenes,et al.  Treatment of green table olive waste waters by an activated‐sludge process , 2000 .

[15]  J. Hoigné Chemistry of Aqueous Ozone and Transformation of Pollutants by Ozonation and Advanced Oxidation Processes , 1998 .