Accurately determining the shaft power consumption is
important
in the design and scale-up of stirred tanks with particles. Firstly,
the apparent viscosity of the stirring particles
is proposed. The effects of impeller type, agitation speed, and particle
filling level on the apparent viscosity of the stirring
particles are experimentally studied with various particles. It was
found that larger particles, a greater friction coefficient between
particles, and a higher particle filling level all result in a larger apparent viscosity of the particles. The stirred particles
show shear thinning behavior, which is similar to the pseudoplastic
non-Newtonian fluids. Finally, based on the force analysis and the
concept of particles having an apparent viscosity, a model predicting the shaft power consumption in stirring noncohesive
particles is proposed. The predicted shaft power in the stirred tank
is within ±15% with particles of different sizes. When the model
is applied to the 10-times scaled-up stirred tank with geometric similarity,
the prediction results of the shaft power are within ±6%.