One of the main difficulties in modelling a Fluidized Bed Biofilm Reactor (FBBR) is to take into account hydraulic phenomena (such as bed expansion) and its interactions with the biological variables. In this paper, we shall present a dynamical model of the process, analyse the stability of the hydrodynamics and illustrate its performances in simulation, A key feature of the model is that it combines mass balance of the process components with momentum balance equations in order to emphasise the different hydrodynamics of the liquid phase and of the solid phase, and the interactions between both phases, The model derivation finally leads to a set of partial differential equations (PDE), This model is intended to be used as a basis for the d...
A mathematical model of a high-rate anaerobic treatment system was developed by defining the biologi...
The paper presents a mathematical model able to simulate under dynamic conditions the physical, chem...
This paper proposes to extend the dynamical analysis results on chemical tubular reactors presented ...
The main purpose of this paper is to analyze the adequacy of some hypotheses assumed in the literatu...
The main purpose of this paper was to present a heterogeneous model of a three-phase solid-liquid-ga...
Abstract -This work presents an experimental and theoretical investigation of anaerobic fluidized be...
The main purpose of this paper is to present a model of a three-phase solid-liquid-gas system to inv...
A mathematical model for anaerobic digestion in plug-flow reactors is proposed on the basis of mass ...
In this work, we focus on the anaerobic digestion model no 1 proposed by I.W.A. working group (Batst...
This work presents an experimental and theoretical investigation of anaerobic fluidized bed reactors...
Doctorat internacionalAnaerobic digestion is one of the most widely used biological treatments for t...
In this paper, we propose a new model for control purposes in coupling a simple membrane fouling dyn...
Biofilm models, developed by previous researchers, were incorporated with an equilibrium model to st...
A dynamical model of a continuous biofilm reactor is presented. The reactor consists of a three-phas...
In the recent years, there has been an increasing interest in the development of hybrid reactors, es...
A mathematical model of a high-rate anaerobic treatment system was developed by defining the biologi...
The paper presents a mathematical model able to simulate under dynamic conditions the physical, chem...
This paper proposes to extend the dynamical analysis results on chemical tubular reactors presented ...
The main purpose of this paper is to analyze the adequacy of some hypotheses assumed in the literatu...
The main purpose of this paper was to present a heterogeneous model of a three-phase solid-liquid-ga...
Abstract -This work presents an experimental and theoretical investigation of anaerobic fluidized be...
The main purpose of this paper is to present a model of a three-phase solid-liquid-gas system to inv...
A mathematical model for anaerobic digestion in plug-flow reactors is proposed on the basis of mass ...
In this work, we focus on the anaerobic digestion model no 1 proposed by I.W.A. working group (Batst...
This work presents an experimental and theoretical investigation of anaerobic fluidized bed reactors...
Doctorat internacionalAnaerobic digestion is one of the most widely used biological treatments for t...
In this paper, we propose a new model for control purposes in coupling a simple membrane fouling dyn...
Biofilm models, developed by previous researchers, were incorporated with an equilibrium model to st...
A dynamical model of a continuous biofilm reactor is presented. The reactor consists of a three-phas...
In the recent years, there has been an increasing interest in the development of hybrid reactors, es...
A mathematical model of a high-rate anaerobic treatment system was developed by defining the biologi...
The paper presents a mathematical model able to simulate under dynamic conditions the physical, chem...
This paper proposes to extend the dynamical analysis results on chemical tubular reactors presented ...