2008
DOI: 10.2202/1542-6580.1449
|View full text |Cite
|
Sign up to set email alerts
|

Modelling Three-Phase Fluidized Bed Bioreactor for Wastewater Treatment

Abstract: Economically and technically interesting, the bioreactor phenomena are studied on both micro (pore and particle size) and macro (bioreactor) levels, to describe synergetic between bio-dynamics and physicochemical dynamics. Still, the three-phase bioreactors modelling remains complex. It requires taking into account numerous factors: the pollutant biodegradation rate in the biofilm, the reactant interfacial gas-liquid and liquid-solid mass transfer, the biofilm composition and growth, the granular structure … Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1

Citation Types

0
2
0

Year Published

2011
2011
2021
2021

Publication Types

Select...
3
1

Relationship

0
4

Authors

Journals

citations
Cited by 4 publications
(2 citation statements)
references
References 15 publications
0
2
0
Order By: Relevance
“…Several different types of biofilm reactors have been studied, including rotating disk bioreactors, fixed bed reactors and three phase fluidized bed bioreactors. The latter are considered superior because of large biofilm support surfaces, appropriate hydrodynamic conditions, high mass transfer rates of both oxygen and substrate and excellent contact between the liquid and solid phases (Schugerl, 1997;Reese et al, 1999;Boumehdi Toumi et al, 2008;Daugulis, 2011). However, one significant problem in practically all types of biofilm reactors, including fluidized-bed reactors, is uncontrolled biofilm growth Korpal, 2004, 2006), which limits the diffusion of oxygen and/or the organic substrate to the deeper layers of the biofilm.…”
Section: Introductionmentioning
confidence: 99%
“…Several different types of biofilm reactors have been studied, including rotating disk bioreactors, fixed bed reactors and three phase fluidized bed bioreactors. The latter are considered superior because of large biofilm support surfaces, appropriate hydrodynamic conditions, high mass transfer rates of both oxygen and substrate and excellent contact between the liquid and solid phases (Schugerl, 1997;Reese et al, 1999;Boumehdi Toumi et al, 2008;Daugulis, 2011). However, one significant problem in practically all types of biofilm reactors, including fluidized-bed reactors, is uncontrolled biofilm growth Korpal, 2004, 2006), which limits the diffusion of oxygen and/or the organic substrate to the deeper layers of the biofilm.…”
Section: Introductionmentioning
confidence: 99%
“…(3) Intimate contact between the liquid and solid phases is achieved. (4) The use of supporting particles allows the partial replenishment of the fluidized bed without interrupting the operation in order to maintain high microbial activity [2].…”
mentioning
confidence: 99%