Numerical Studies of the Gas-Solid Hydrodynamics at High Temperature in the Riser of a Bench-Scale Circulating Fluidized Bed : Table 1

Table 1: Geometrical and physical properties of the system.


Riser internal diameter,	0.102 m
Standpipe/L-valve diameter,	0.063 m
Riser height, H	4.0 m
Particle density,	2,700 kg/m³
Particle Sauter mean diameter,	353 μm
Particle specific heat,	830 J/kg K
Minimum fluidization velocity¹,	0.06 m/s
Particle transport velocity²,	5.78 m/s
Particle Geldart group	B

¹Wen and Yu [28]; ²Bai et al. [29].