ISSN:
0006-3592
Keywords:
Chemistry
;
Biochemistry and Biotechnology
Source:
Wiley InterScience Backfile Collection 1832-2000
Topics:
Biology
,
Process Engineering, Biotechnology, Nutrition Technology
Notes:
Bed fluidization offers the possibility of gaining the advantages of fixed-film biological processes without the disadvantage of pore clogging. However, the biofilm detachment rate, due to hydrodynamics and particle-to-particle attrition, is very poorly understood for fluidized-bed biofilm processes. In this work, a two-phase fluidized-bed biofilm was operated under a constant surface loading (0.09 mg total organic carbon/cm2 day) and with a range of bed height (H), fluid velocities (U), and support-particle concentrations (Cp). Direct measurements were made for the specific biofilm loss rate coefficient (bs)and the total biofilm accumulation (XfLf). A hydrodynamic model allowed independent determination of the biofilm density (Xf), biofilm thickness (Lf), liquid shear stress (τ), and Reynolds number (Re). Multiple regression analysis of the results showed that increased particle-to-particle attrition, proportional to Cp and increased turbulence, described by Re, caused the biofilms to be denser and thinner. The specific detachment rate coefficient (bs) increased as Cp and Re increased. Almost all of the 6, values were larger than predicted by a previous model derived for smooth biofilms on a nonfluidized surface. Therefore, the turbulence and attrition of bed fluidization appear to be dominant detachment mechanisms.
Additional Material:
6 Ill.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1002/bit.260380508
Permalink
