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  • 1
    ISSN: 1572-9729
    Keywords: biodegradation ; growth inhibition ; metabolites ; toluene ; xylenes
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Energy, Environment Protection, Nuclear Power Engineering , Agriculture, Forestry, Horticulture, Fishery, Domestic Science, Nutrition
    Notes: Abstract A biomass adapted to degrade toluene and xylenes in mixture was grown in a batch reactor with substrates supplied by pulses. The inhibition of biomass growth in the course of substrate degradation was investigated. The maximal biomass concentration of 7 g l−1 was obtained using 150 μl of toluene and 15 μl of a mixture of xylenes in one litre of liquid medium, and the maximal biomass productivity and yield were 53 mg l−1 h−1 and 0.32 gDW g s −1 , respectively. Higher quantities of substrate added by pulses, that is 200 μl of toluene with 20 μl of xylenes and 300 μl of toluene with 30 μl of xylenes, caused an accumulation of metabolites. These higher quantities of substrates caused inhibition of microbial growth. Among the metabolites produced, 4-methyl catechol was found in large quantities in the culture medium and in the cells.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Chichester : Wiley-Blackwell
    Journal of Chemical Technology AND Biotechnology 71 (1998), S. 84-88 
    ISSN: 0268-2575
    Keywords: biofilm ; industrial wastewater ; segmented column ; biokinetic parameters ; mass transfer ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: This study describes a technique for estimating biokinetic and mass transfer parameters for biofilm processes in wastewater treatment. The reactor used consisted of a column divided into separate units packed with expanded clay pellets. Samples were taken at the exit of each unit. Oxygen mass transfer and oxygen consumption rate were determined. The system was operated with cocurrent upflows of air and industrial wastewater. A mathematical approach was developed to estimate biokinetic parameters such as the maximal oxygen removal rate, saturation constant and internal diffusion coefficient. © 1998 SCI.
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
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