Experiments were conducted comparing mixing performance in a conventional d
ouble-cone blender and in a double-cone blender that was modified by means
of a stationary deflector plate in order to enhance axial particle flow. Mi
xing performance was assessed qualitatively using a transparent mixing vess
el to visualize particle mixing patterns and determine the state of homogen
eity at the mixture's surface during the entire experiment. Mixing performa
nce was also examined quantitatively by repeatedly vacuuming several layers
of beads, taking a digital image of the bed after vacuuming, and using ima
ge analysis to subdivide the images into samples and determine the composit
ion of each sample. The effect of operating conditions (rotation rate, vess
el fill percentage and total number of revolutions) was examined. Mixing wa
s quantified in terms of the standard deviation of the concentration of a t
racer. The evolution of the process was accurately described by a single-pa
rameter model that characterized axial mixing as a first order process with
a characteristic rate constant. For double-cone mixers of standard design,
under all operating conditions, slow flow of particles through a vertical
plane of symmetry at the center of the vessel caused poor mixing performanc
e, insertion of a deflector plate inclined relative to this plane was very
effective in enhancing mixing. The effect of the deflector was to create a
convective axial flow across the center of the mixer, increasing the mixing
rate by a factor of 25:1. (C) 2000 Elsevier Science S.A. All rights reserv
ed.