CFD-calculation of flow, dispersion and reaction in a catalyst filled tubeby the lattice Boltzmann method

Citation
T. Zeiser et al., CFD-calculation of flow, dispersion and reaction in a catalyst filled tubeby the lattice Boltzmann method, CHEM ENG SC, 56(4), 2001, pp. 1697-1704
Citations number
38
Categorie Soggetti
Chemical Engineering
Journal title
CHEMICAL ENGINEERING SCIENCE
ISSN journal
00092509 → ACNP
Volume
56
Issue
4
Year of publication
2001
Pages
1697 - 1704
Database
ISI
SICI code
0009-2509(200102)56:4<1697:COFDAR>2.0.ZU;2-R
Abstract
The behaviour of a reacting, viscous flow inside the complex geometry of a fixed-bed reactor has been studied by means of a lattice Boltzmann automata (LBA). In particular, two tasks have been investigated in detail. The geom etrical structures of the fixed bed have been generated with a Monte-Carlo method. This allows to simulate very efficiently the placement of randomly packed spheres in a cylinder and to obtain detailed information of statisti cal properties, such as the voidage distribution. This geometrical informat ion is the base for the subsequent numerical flow simulation using a lattic e Boltzmann automata. This approach allows to predict the local fluid veloc ity distribution in the bed as well as the transport and reactions of chemi cal species taking into account the effect of heterogeneous catalysis. Thus , detailed information can be provided for the diffusion/dispersion effects around catalytic particles and ensembles of spheres. It is shown that this approach allows to improve the understanding of the underlying transport a nd reaction phenomena in these reactors and to obtain a reliable database f or their operating behaviour and design. (C) 2001 Elsevier Science Ltd. All rights reserved.