TY - JOUR
T1 - CFD study of local crystal growth rate in a continuous suspension crystallizer
AU - Mori, Yuko
AU - Sha, Zuoliang
AU - Louhi-Kultanen, Marjatta
AU - Kallas, Juha
PY - 2002/11
Y1 - 2002/11
N2 - The objective of the present work is to determine the local crystal growth rate in an imperfectly mixed suspension crystallizer. Experiments were carried out in pure potassium sulphate-water solution. The steady-state Crystal Size Distributions (CSDs) were measured at four different heights of the crystallizer using an in-situ particle image analyzer. Experimentally obtained CSD was used to determine the overall growth rate. Then, Computational Fluid Dynamics (CFD) was used to calculate the Particle Size Distributions (PSDs) of the same kind of suspension which was used in the experiments. The computational study was focused to simulate the mass transfer coefficient between particles and solution, and supersaturation, These quantities were determined from hydrodynamics of suspension in a crystallizer. The multi-fluid model was applied to describe suspension flow in the crystallizer. One continuous phase (water) and six dispersed phases, which were taken to be particles in six size classes, were used to approximate PSD. The crystal growth rate model was based on the diffusion process and was implemented into a CFD environment. The local growth rates were calculated from the slip velocity or from energy dissipation rate at the local temperature and supersaturation.
AB - The objective of the present work is to determine the local crystal growth rate in an imperfectly mixed suspension crystallizer. Experiments were carried out in pure potassium sulphate-water solution. The steady-state Crystal Size Distributions (CSDs) were measured at four different heights of the crystallizer using an in-situ particle image analyzer. Experimentally obtained CSD was used to determine the overall growth rate. Then, Computational Fluid Dynamics (CFD) was used to calculate the Particle Size Distributions (PSDs) of the same kind of suspension which was used in the experiments. The computational study was focused to simulate the mass transfer coefficient between particles and solution, and supersaturation, These quantities were determined from hydrodynamics of suspension in a crystallizer. The multi-fluid model was applied to describe suspension flow in the crystallizer. One continuous phase (water) and six dispersed phases, which were taken to be particles in six size classes, were used to approximate PSD. The crystal growth rate model was based on the diffusion process and was implemented into a CFD environment. The local growth rates were calculated from the slip velocity or from energy dissipation rate at the local temperature and supersaturation.
KW - CFD
KW - Crystal growth rate
KW - Crystal size distribution
KW - Mass transfer
KW - Suspension crystallization
UR - http://www.scopus.com/inward/record.url?scp=0036870218&partnerID=8YFLogxK
U2 - 10.1252/jcej.35.1178
DO - 10.1252/jcej.35.1178
M3 - Article
AN - SCOPUS:0036870218
SN - 0021-9592
VL - 35
SP - 1178
EP - 1187
JO - JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
JF - JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
IS - 11
ER -