TY - JOUR
T1 - Double-diffusive mixed convection of pseudoplastic fluids in a two sided lid-driven cavity using FDLBM
AU - Kefayati, Gholamreza
PY - 2014
Y1 - 2014
N2 - In this paper, mixed convection of shear-thinning fluids in a two sided square lid-driven cavity under the combined buoyancy effects of thermal and mass diffusion has been analyzed by Finite Difference Lattice Boltzmann method (FDLBM). This study has been conducted for the certain pertinent parameters of Richardson number (Ri=0.00062-1), Lewis number (Le=5 and 10), power-law index (n=0.2-1) as the buoyancy ratio is studied from N=-20 to 20. It should be mentioned the Reynolds number has been studied at Re=10, 100 and 400 as the thermal Grashof number is fixed at GrT=100. Results indicate that the augmentation of Richardson number decreases heat and mass transfer. The fall of the power law index declines heat and mass transfer at Ri=0.00062 and 0.01. At Ri=1, the heat and mass transfer rises with the drop of power-law index for buoyancy ratios of N=-20 and 20.The least effect of power-law index on heat and mass transfer among the studied Richardson numbers was observed at Ri=1 for N=1.The growth of Lewis number enhances the mass transfer for different buoyancy ratios as it declines the effect of power-law index on the mass transfer at N=20 and -20.
AB - In this paper, mixed convection of shear-thinning fluids in a two sided square lid-driven cavity under the combined buoyancy effects of thermal and mass diffusion has been analyzed by Finite Difference Lattice Boltzmann method (FDLBM). This study has been conducted for the certain pertinent parameters of Richardson number (Ri=0.00062-1), Lewis number (Le=5 and 10), power-law index (n=0.2-1) as the buoyancy ratio is studied from N=-20 to 20. It should be mentioned the Reynolds number has been studied at Re=10, 100 and 400 as the thermal Grashof number is fixed at GrT=100. Results indicate that the augmentation of Richardson number decreases heat and mass transfer. The fall of the power law index declines heat and mass transfer at Ri=0.00062 and 0.01. At Ri=1, the heat and mass transfer rises with the drop of power-law index for buoyancy ratios of N=-20 and 20.The least effect of power-law index on heat and mass transfer among the studied Richardson numbers was observed at Ri=1 for N=1.The growth of Lewis number enhances the mass transfer for different buoyancy ratios as it declines the effect of power-law index on the mass transfer at N=20 and -20.
KW - FDLBM
KW - Mass transfer
KW - Mixed convection
KW - Pseudoplastic fluids
UR - http://www.scopus.com/inward/record.url?scp=84922443860&partnerID=8YFLogxK
U2 - 10.1016/j.jtice.2014.05.026
DO - 10.1016/j.jtice.2014.05.026
M3 - Article
SN - 1876-1070
VL - 45
SP - 2122
EP - 2139
JO - Journal of the Taiwan Institute of Chemical Engineers
JF - Journal of the Taiwan Institute of Chemical Engineers
IS - 5
ER -