Significance of fluid regime and wetted area in biofilm reactors


Muslu Y.

APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, vol.101, no.3, pp.177-195, 2002 (Journal Indexed in SCI) identifier identifier identifier

  • Publication Type: Article / Article
  • Volume: 101 Issue: 3
  • Publication Date: 2002
  • Doi Number: 10.1385/abab:101:3:177
  • Title of Journal : APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY
  • Page Numbers: pp.177-195

Abstract

Mass transfer within microbial films was described using Monod-type biological kinetics in terms of properties of filter media and feed solution. The performance characteristics of a trickling filter were thus modeled. The model enables one to consider the effect of inlet substrate concentration and flow rate upon the removal efficiency. For this purpose a second-order partial differential equation describing the dispersion phenomena inside the liquid layer was solved under special boundary conditions and used to determine substrate flux into the biofilm. A uniform biofilm thickness was considered. The model is based on computer techniques and the numerical evaluation of the normalized biofilm mathematical model. A design procedure was also given to calculate biological filters. The numerical model was also applied to experimental data to demonstrate its validity.