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      Net growth rate of continuum heterogeneous biofilms with inhibition kinetics

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          Abstract

          Biofilm systems can be modeled using a variety of analytical and numerical approaches, usually by making simplifying assumptions regarding biofilm heterogeneity and activity as well as effective diffusivity. Inhibition kinetics, albeit common in experimental systems, are rarely considered and analytical approaches are either lacking or consider effective diffusivity of the substrate and the biofilm density to remain constant. To address this obvious knowledge gap an analytical procedure to estimate the effectiveness factor (dimensionless substrate mass flux at the biofilm-fluid interface) was developed for a continuum heterogeneous biofilm with multiple limiting-substrate Monod kinetics to different types of inhibition kinetics. The simple perturbation technique, previously validated to quantify biofilm activity, was applied to systems where either the substrate or the inhibitor is the limiting component, and cases where the inhibitor is a reaction product or the substrate also acts as the inhibitor. Explicit analytical equations are presented for the effectiveness factor estimation and, therefore, the calculation of biomass growth rate or limiting substrate/inhibitor consumption rate, for a given biofilm thickness. The robustness of the new biofilm model was tested using kinetic parameters experimentally determined for the growth of Pseudomonas putida CCRC 14365 on phenol. Several additional cases have been analyzed, including examples where the effectiveness factor can reach values greater than unity, characteristic of systems with inhibition kinetics. Criteria to establish when the effectiveness factor can reach values greater than unity in each of the cases studied are also presented.

          Biofilm growth: Investigating inhibition

          A method to model and assess the effect of interactions and processes that inhibit biofilm growth closes a gap in understanding. Biofilm growth is often inhibited by chemicals used or produced by microorganisms, or by other components and characteristics of the surroundings. This has been a neglected aspect of the procedures used to analyze and predict biofilm behavior. Stefan Wuertz at Nanyang Technological University in Singapore, with colleagues in Singapore and Argentina, mathematically modeled these often-overlooked inhibitory effects. They tested the accuracy of their procedure on complex biofilms under a variety of growing conditions. The insights gained into growth inhibition should help with the design of bioreactors, including those used to degrade pollutants. The method should be widely applicable to all types of biofilms, ranging from laboratory to industrial scale applications.

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          Most cited references22

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          Substrate and product inhibition kinetics in succinic acid production by Actinobacillus succinogenes

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            The monod equation: A revisit and a generalization to product inhibition situations

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              Evaluation and modeling of benzalkonium chloride inhibition and biodegradation in activated sludge.

              The inhibitory effect and biodegradation of benzalkonium chloride (BAC), a mixture of alkyl benzyl dimethyl ammonium chlorides with different alkyl chain lengths, was investigated at a concentration range from 5 to 20 mg/L and different biomass concentrations in an activated sludge system. A solution containing glucose and mineral salts was used as the wastewater in all the assays performed. The inhibition of respiratory enzymes was identified as the mode of action of BAC as a result of oxygen uptake rate analysis performed at BAC concentrations ranging between 5 and 70 mg/L. The glucose degradation in the activated sludge at different BAC and biomass concentrations was well-described with Monod kinetics with competitive inhibition. The half-saturation inhibition constant (K(I)) which is equivalent to EC(50) of BAC for the activated sludge tested ranged between 0.12 and 3.60 mg/L. The high K(I) values were recorded at low BAC-to-biomass ratios, i.e. less than 10 mg BAC/g VSS, at which BAC was almost totally adsorbed to biomass and not bioavailable. BAC degradation started as soon as glucose was totally consumed. Although BAC was almost totally adsorbed on the biomass, it was degraded completely. Therefore, BAC degradation was modeled using two-phase biodegradation kinetics developed in this study. This model involves rapid partitioning of BAC to biomass and consecutive degradation in both aqueous and solid phases. The aqueous phase BAC degradation rate was twenty times, on average, higher than the solid phase degradation rate. The specific aqueous (k(I1)) and solid (k(I2)) phase BAC utilization rate constants were 1.25 and 0.31 mg BAC/g VSS h, respectively. The findings of this study would help to understand the reason of extensive distribution of quaternary ammonium compounds in wastewater treatment plant effluents and in natural water systems although QACs are biodegradable, and develop strategies to avoid their release and accumulation in the environment.
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                Author and article information

                Contributors
                swuertz@ntu.edu.sg
                Journal
                NPJ Biofilms Microbiomes
                NPJ Biofilms Microbiomes
                NPJ Biofilms and Microbiomes
                Nature Publishing Group UK (London )
                2055-5008
                8 March 2018
                8 March 2018
                2018
                : 4
                : 5
                Affiliations
                [1 ]ISNI 0000 0004 0490 9553, GRID grid.10821.3a, INIQUI (CONICET)—Facultad de Ingeniería, , Universidad Nacional de Salta, ; Av. Bolivia 5150, Salta, 4400 Argentina
                [2 ]ISNI 0000 0001 2224 0361, GRID grid.59025.3b, Singapore Centre for Environmental Life Sciences Engineering (SCELSE), , Nanyang Technological University, ; Singapore, 637551 Singapore
                [3 ]ISNI 0000 0001 2224 0361, GRID grid.59025.3b, School of Civil and Environmental Engineering, , Nanyang Technological University, ; Singapore, 639798 Singapore
                Article
                45
                10.1038/s41522-017-0045-y
                5843665
                038d6f7d-52e6-4b15-9e70-5b062d3a63e7
                © The Author(s) 2018

                Open Access This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The images or other third party material in this article are included in the article’s Creative Commons license, unless indicated otherwise in a credit line to the material. If material is not included in the article’s Creative Commons license and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this license, visit http://creativecommons.org/licenses/by/4.0/.

                History
                : 4 June 2017
                : 2 December 2017
                : 5 December 2017
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                © The Author(s) 2018

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