CFD-PBM Coupled Simulation of Liquid-Liquid Dispersions in Spray Fluidized Bed Extractor: Comparison of Three Numerical Methods

Table 4

Model parameter.

Parameter	Value
Inlet condition	Velocity inlet
Outlet condition	Pressure outlet
Wall condition	No slip for oil
	Free slip for liquid
Inlet turbulent intensity	0.0064 m^2s^−2
Inlet hydraulic diameter	0.01 m
Operating density	800 kgm^−3
Continuous phase density	998 kgm^−3
Disperse phase density	800 kgm^−3
Granular temperature	0.0001 m^2s^−2
Inlet velocity	0.9 ms^−1
Diameter	Sauter
Continuous phase viscosity	0.0012 kgm^−1s^−1
Disperse phase viscosity	0.0089 kgm^−1s
Back volume fraction	1
Operating pressure	101325 pa
Inlet turbulent dissipation rate	0.009 m^2s^−2
Inlet turbulent kinetic energy	0.24 m^2s^−3