The continuum heterogeneous biofilm model with multiple limiting substrate Monod kinetics.
| dc.contributor.author | Gonzo, Elio Emilio | |
| dc.contributor.author | Wuertz, Stefan | |
| dc.contributor.author | Rajal, Veronica B | |
| dc.coverage.spatial | Bolivia | |
| dc.date.accessioned | 2026-03-24T15:06:55Z | |
| dc.date.available | 2026-03-24T15:06:55Z | |
| dc.date.issued | 2014 | |
| dc.description | Vol. 111, No. 11, pp. 2252-64 | |
| dc.description.abstract | We describe a novel procedure to estimate the net growth rate of biofilms on multiple substrates. The approach is based on diffusion-reaction mass balances for chemical species in a continuum biofilm model with reaction kinetics corresponding to a Double-Monod expression. This analytical model considers a heterogeneous biofilm with variable distributions of biofilm density, activity, and effective diffusivity as a function of depth. We present the procedure to estimate the effectiveness factor analytically and compare the outcome with values obtained by the application of a rigorous numerical computational method using several theoretical examples and a test case. A comparison of the profiles of the effectiveness factor as a function of the Thiele modulus, φ, revealed that the activity of a homogeneous biofilm could be as much as 42% higher than that of a heterogeneous biofilm, under the given conditions. The maximum relative error between numerical and estimated effectiveness factor was 2.03% at φ near 0.7 (corresponding to a normalized Thiele modulus φ* = 1). For φ < 0.3 or φ > 1.4, the relative error was less than 0.5%. A biofilm containing aerobic ammonium oxidizers was chosen as a test case to illustrate the model's capability. We assumed a continuum heterogeneous biofilm model where the effective diffusivities of oxygen and ammonium change with biofilm position. Calculations were performed for two scenarios; Case I had low dissolved oxygen (DO) concentrations and Case II had high DO concentrations, with a concentration at the biofilm-fluid interface of 10 g O2 /m(3) . For Case II, ammonium was the limiting substrate for a biofilm surface concentration, CNs , ≤13.84 g of N/m(3) . At these concentrations ammonium was limiting inside the biofilm, and oxygen was fully penetrating. Conversely, for CNs > 13.84 g of N/m(3) , oxygen became the limiting substrate inside the biofilm and ammonium was fully penetrating. Finally, a generalized procedure to estimate the effectiveness factor for a system with multiple (n > 2) limiting substrates is given. | eng |
| dc.description.sponsorship | INIQUI (CONICET)-Facultad de Ingeniería, Universidad Nacional de Salta, Av. Bolivia 5150, Salta, 4400, Argentina. | |
| dc.identifier.doi | 10.1002/bit.25284 | |
| dc.identifier.issn | 1097-0290 | |
| dc.identifier.other | PMID:24888450 | |
| dc.identifier.uri | https://doi.org/10.1002/bit.25284 | |
| dc.identifier.uri | https://andeanlibrary.org/handle/123456789/101285 | |
| dc.language.iso | eng | |
| dc.relation.ispartof | Biotechnology and bioengineering | |
| dc.source | PubMed | |
| dc.subject | Monod kinetics | |
| dc.subject | biofilm model | |
| dc.subject | continuum heterogeneous biofilm | |
| dc.subject | effectiveness factor | |
| dc.subject | multiple-substrate limitation | |
| dc.title | The continuum heterogeneous biofilm model with multiple limiting substrate Monod kinetics. | |
| dc.type | Artículo Científico Publicado |