Abstract
The dimensionless steady-state flux, J*, of substrate into a biofilm can be expressed as a function of the concentration of substrate in the bulk, Sb*, the thickness of the stagnant liquid layer surrounding the biofilm, L*, and the minimum concentration of substrate capable of sustaining growth, Smin*. Using a simplified algebraic expression that relates J* to Sb*, L* and Smin*, a series of nomograms were developed that give the performance of completely mixed (fluidized-bed) and plug-flow (packed-bed) biofilm reactors as a function of process parameters such as hydraulic retention time, kinetic constants and hydrodynamic conditions. The nomograms are simple to use and provide a tool for analyzing the performance of such reactors based in fundamental principles.
| Original language | English |
|---|---|
| Pages (from-to) | 837-844 |
| Number of pages | 8 |
| Journal | Water Research |
| Volume | 23 |
| Issue number | 7 |
| DOIs | |
| State | Published - Jul 1989 |
Bibliographical note
Funding Information:Acknowledgement--Funding for this study was provided by the Advanced Environmental Control Technology Research Center, University of Illinois at Urbana--Champaign.
Funding
Acknowledgement--Funding for this study was provided by the Advanced Environmental Control Technology Research Center, University of Illinois at Urbana--Champaign.
Keywords
- attached growth
- biofilm
- design
- expanded-bed
- fluidized-bed
- nomogram
- packed-bed
ASJC Scopus subject areas
- Environmental Engineering
- Civil and Structural Engineering
- Ecological Modeling
- Water Science and Technology
- Waste Management and Disposal
- Pollution
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