Modeling of residence time distribution: Application to a three-phase inverse fluidized bed based on a Mellin transform

被引:11
作者
Montastruc, L. [1 ]
Brienne, J. P. [2 ]
Nikov, I. [1 ]
机构
[1] Univ Lille 1, ProBioGEM, Dept IAAL, Polytech Lille, F-59655 Villeneuve Dascq, France
[2] Univ Lille 1, CNRS, Dept IAAL, LAGIS UMR 8146,Polytech Lille, F-59655 Villeneuve Dascq, France
关键词
RTD; Inverse fluidized bed; Mellin transform; LIQUID; REACTOR; BEHAVIOR;
D O I
10.1016/j.cej.2008.08.035
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The study is focused on modeling of gas and liquid residence time distribution in an aerated liquid system of an inverse fluidized bed bioreactor. Two opposite strategies are currently available: the use of powerful complex Computational fluid dynamics (CFD) simulation and the phenomenological semi-empirical models. In this work, a specific methodology is proposed, as follows: the reactor is modeled as a reactor network containing a combination of zones with basic ideal flow patterns such as perfect mixed flow (PMF) and Plug flow (PF). The approach is based on a Mellin-modification of the Laplace transformation over the relevant equations. The method allows zero-time solutions for identification analysis. The study shows that the increase of the gas flowrate leads to higher mixing intensity of the gas phase. Decreasing the gas velocity, the inverse fluidized bed tends to perform as a plug flow reactor. The liquid phase performs closer to disperse plug flow. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:139 / 144
页数:6
相关论文
共 12 条
[1]   Some hydrodynamic characteristics of inverse three phase fluidized-bed reactors [J].
Buffière, P ;
Moletta, R .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (09) :1233-1242
[2]   Liquid mixing and phase hold-ups in gas producing fluidized bed bioreactors [J].
Buffiere, P ;
Fonade, C ;
Moletta, R .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (04) :617-627
[3]  
Dimitrov D., 2004, BULG CHEM COMMUN, V36, P177
[4]   Local shear and skin friction on particles in three-phase fluidized beds [J].
Essadki, AH ;
Nikov, I ;
Delmas, H .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (22) :6034-6042
[5]   Computer aided synthesis of RTD models to simulate the air flow distribution in ventilated rooms [J].
Laquerbe, C ;
Laborde, JC ;
Soares, S ;
Ricciardi, L ;
Floquet, P ;
Pibouleau, L ;
Domenech, S .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (20) :5727-5738
[6]   Influence of hydrodynamic conditions on biofilm behavior in a methanogenic inverse turbulent bed reactor [J].
Michaud, S ;
Bernet, N ;
Roustan, M ;
Delgenès, JP .
BIOTECHNOLOGY PROGRESS, 2003, 19 (03) :858-863
[7]   A systemic approach for pellet reactor modeling: Application to water treatment [J].
Montastruc, L ;
Azzaro-Pantel, C ;
Pibouleau, L ;
Domenech, S .
AICHE JOURNAL, 2004, 50 (10) :2514-2525
[8]   LIQUID-SOLID MASS-TRANSFER IN INVERSE FLUIDIZED-BED [J].
NIKOV, I ;
KARAMANEV, D .
AICHE JOURNAL, 1991, 37 (05) :781-784
[9]   Biodegradation of aniline using light carriers with optimised surface in TPIFB [J].
Nikov, I ;
Nikolov, V ;
Dimitrov, D .
BIOPROCESS ENGINEERING, 1999, 21 (06) :547-552
[10]  
Pinelli D, 2000, IND ENG CHEM RES, V39, P3202, DOI 10.1021/ie000216+