The microscopic modelling of hydrodynamics in industrial crystallisers

Citation
A. Ten Cate et al., The microscopic modelling of hydrodynamics in industrial crystallisers, CHEM ENG SC, 56(7), 2001, pp. 2495-2509
Citations number
31
Categorie Soggetti
Chemical Engineering
Journal title
CHEMICAL ENGINEERING SCIENCE
ISSN journal
00092509 → ACNP
Volume
56
Issue
7
Year of publication
2001
Pages
2495 - 2509
Database
ISI
SICI code
0009-2509(200104)56:7<2495:TMMOHI>2.0.ZU;2-N
Abstract
In this contribution a method for the calculation of crystal-crystal collis ions in the flow field of an industrial crystalliser is proposed. The metho d consists of two steps. The first step is to simulate the internal Row of the crystalliser as a whole. For this purpose, the simulation of the intern al Row of an 1100 1 draft tube baffled crystalliser at a Reynolds number of 240,000 is presented. This simulation was done with a lattice-Boltzmann sc heme with a Smagorinsky sub-grid-scale turbulence model (c(s) was 0.11) on approximately 35.5 x 10(6) grid nodes. The second step of the method consis ts of simulating individual crystals in a fully periodic box with turbulent conditions that represent the conditions in a point of the crystalliser. T hus collision frequencies and intensities of the crystals under the local h ydrodynamic regime can be obtained. In this contribution a feasibility stud y of this second step is described. A theoretical framework is established to identify the key parameters that determine the relationship between the crystalliser flow and the box simulations. Based on this framework, conditi ons for box simulations representing three monitor points in the simulated crystalliser are calculated. Finally, to demonstrate the method of predicti ng the motion of individual particles, sedimentation and consecutive collis ion of a single sphere with a solid wall is simulated. (C) 2001 Elsevier Sc ience Ltd. All rights reserved.