A chemostat model with variable dilution rate due to biofilm growth
Xiaochen Duan, Sergei S. Pilyugin

TL;DR
This paper introduces a new chemostat model accounting for biofilm growth affecting the fluid volume and dilution rate, revealing diverse dynamic regimes, stability conditions, and potential for multistability and clogging.
Contribution
It develops a novel mathematical model that incorporates biofilm volume increase affecting dilution rate, analyzing its stability and operational regimes.
Findings
The model is well-posed and describes three dynamic regimes.
Conditions for clogging and microbial persistence are identified.
Numerical simulations suggest multistability in the system.
Abstract
In many real life applications, a continuous culture bioreactor may cease to function properly due to bioclogging which is typically caused by the microbial overgrowth. This is a problem that has been largely overlooked in the chemostat modeling literature, despite the fact that a number of models explicitly accounted for biofilm development inside the bioreactor. In a typical chemostat model, the physical volume of the biofilm is considered negligible when compared to the volume of the fluid. In this paper, we investigate the theoretical consequences of removing such assumption. Specifically, we formulate a novel mathematical model of a chemostat where the increase of the biofilm volume occurs at the expense of the fluid volume of the bioreactor, and as a result the corresponding dilution rate increases reciprocally. We show that our model is well-posed and describes the bioreactor…
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Taxonomy
TopicsWastewater Treatment and Nitrogen Removal · Odor and Emission Control Technologies
