2008
DOI: 10.1016/j.watres.2008.09.037
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Modelling the production and degradation of soluble microbial products (SMP) in membrane bioreactors (MBR)

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Cited by 156 publications
(90 citation statements)
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References 45 publications
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“…The physical sub-model describes the key processes occurring during membrane physical separation, including membrane fouling (involving 6 model factors and 2 state variables). Regarding, the biological sub-models they are based both on the ASM2d and they include the SMP formation/degradation processes (Jiang et al 2008;Henze et al 2000). Furthermore, both models take into account CO 2 as state variable according to the continuity-based model interface as proposed by Vanrolleghem et al (2005).…”
Section: Mathematical Models Descriptionmentioning
confidence: 99%
“…The physical sub-model describes the key processes occurring during membrane physical separation, including membrane fouling (involving 6 model factors and 2 state variables). Regarding, the biological sub-models they are based both on the ASM2d and they include the SMP formation/degradation processes (Jiang et al 2008;Henze et al 2000). Furthermore, both models take into account CO 2 as state variable according to the continuity-based model interface as proposed by Vanrolleghem et al (2005).…”
Section: Mathematical Models Descriptionmentioning
confidence: 99%
“…In particular, the integrated MBR model is able to simulate the phosphorus removal process, often neglected in the modelling literature [7]. The model was developed during previous studies [10,24]; in the following, the model structure is briefly presented.…”
Section: Model Description and Case Studymentioning
confidence: 99%
“…kinetics, stoichiometry and fractionation coefficients). For the variables, process and parameter descriptions, the reader is referred to the literature [10,24]. The biological sub-model simulates the biological nutrient removal processes occurring in a UCT-MBR system and the SMPs formation/degradation.…”
Section: Model Description and Case Studymentioning
confidence: 99%
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“…The need to widen the model boundaries and to include other process units led to the development of several other models such as ADM1 for anaerobic treatment (Batstone et al 2002), fixed biomass (Rittmann & McCarty 1980;Wanner & Gujer 1986;Horn et al 2003) and membrane bioreactors (MBRs; Lu et al 2001;Jiang et al 2008). Nitrite as an intermediate compound is included in several models (Sin et al 2008).…”
Section: Introductionmentioning
confidence: 99%