F. Bose et al., HYDRODYNAMICS OF DISPERSED LIQUID DROPLETS IN AGITATED SYNTHETIC FIBROUS SLURRIES, Industrial & engineering chemistry research, 36(11), 1997, pp. 5028-5036
The hydrodynamic and liquid particle dispersion processes in agitated
vessels containing dilute liquid-liquid dispersions, and dilute liquid
dispersions in synthetic fibrous slurries, were experimentally studie
d, A transparent cylindrical vessel 25 cm in height and 15.5 cm in dia
meter equipped with a six-blade impeller, with geometric proportions r
epresenting the standard vessel configuration, was used. The steady-st
ate size distributions of molten wax particles, which constituted 1% b
y weight of the mixture everywhere, in pure water, and in aqueous slur
ries with 0.1%, 0.5%, 0.8%, and 1.0% consistencies of nylon fibers, we
re measured using sampling and microscopic image analyses, The average
nylon fiber length and diameter were 6.22 mm and 19.5 mu m, respectiv
ely. With pure water the molten wax particle size distributions were s
patially homogeneous and bimodal everywhere and confirmed locally isot
ropic turbulence in the vessel. In tests with fibrous slurries, for fi
ber consistencies smaller than 1%, the molten wax particle size distri
butions remained spatially homogeneous and agreed with the locally iso
tropic turbulence assumption. However, they were unimodal everywhere w
ith narrow particle diameter spectra. Increasing the fiber-consistency
and impeller speed both lead to smaller mean molten wax particles and
narrower particle diameter ranges, suggesting that fibers hamper part
icle collision and coalescence. With 1% fiber consistency, widespread
flow stratification and fiber flocculation took place.