dc.creatorGonzo, Elio Emilio
dc.creatorWuertz, Stefan
dc.creatorRajal, Verónica Beatriz
dc.date.accessioned2016-03-11T19:32:57Z
dc.date.accessioned2018-11-06T11:44:59Z
dc.date.available2016-03-11T19:32:57Z
dc.date.available2018-11-06T11:44:59Z
dc.date.created2016-03-11T19:32:57Z
dc.date.issued2014-11
dc.identifierGonzo, Elio Emilio; Wuertz, Stefan; Rajal, Verónica Beatriz; The Continuum Heterogeneous Biofilm Model With Multiple Limiting Substrate Monod Kinetics; Wiley; Biotechnology and Bioengineering; 111; 11; 11-2014; 2252-2264
dc.identifier1097-0290
dc.identifierhttp://hdl.handle.net/11336/4742
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1859071
dc.description.abstractWe 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/m3. For Case II, ammonium was the limiting substrate for a biofilm surface concentration, CNs, ≤13.84 g of N/m3. At these concentrations ammonium was limiting inside the biofilm, and oxygen was fully penetrating. Conversely, for CNs > 13.84 g of N/m3, 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.
dc.languageeng
dc.publisherWiley
dc.relationinfo:eu-repo/semantics/altIdentifier/url/http://onlinelibrary.wiley.com/wol1/doi/10.1002/bit.25284/abstract
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1002/bit.25284
dc.relationinfo:eu-repo/semantics/altIdentifier/issn/1097-0290
dc.rightshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.rightsinfo:eu-repo/semantics/restrictedAccess
dc.subjectBIOFILM
dc.subjectCONTINUUM HETEROGENEPOUS MODEL
dc.subjectMULTIPLE SUBSTRATE MONOD KINETICS
dc.titleThe Continuum Heterogeneous Biofilm Model With Multiple Limiting Substrate Monod Kinetics
dc.typeArtículos de revistas
dc.typeArtículos de revistas
dc.typeArtículos de revistas


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