A study of substrate removal in a microbial film reactor

A mathematical model is formulated describing the mechanism of substrate removal by a microbial slime over which a film of liquid, containing the substrate as dissolved biodegradable material, is flowing. It is assumed that a lack of either organic carbon, oxygen, or both simultaneously, can limit the overall rate of the process. Basic chemical engineering principles of interfacial mass transfer, diffusion and biochemical reaction are used in the formulation of the model and the resulting set of equations is solved by digitial computer using typical kinetic parameters taken from the literature. Predictions of whether organic carbon, oxygen, or both simultaneously, limit the process, the substrate removal rate, and the active depth of the biofilm are made. Data were obtained in support of the model by measuring substrate removals on a vertically mounted experimental biofilm reactor over a range of hydraulic and organic loadings typical of industrial-scale operation.

Grantor dc:publisher.institution

Department of Chemical Engineering

Year dc:date.issued

1975

Author dc:creator

• Harris, Nicholas Paul

Advisor dc:contributor.advisor

• Hansford, Geoffrey Spearing

Language dc:language.iso

eng

Handle dc:identifier.uri

http://hdl.handle.net/11427/12311

OAI identifier oai:identifier

oai:open.uct.ac.za:11427/12311