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Elucidation of polyurethane dispersions in a batch rotor-stator mixer
Authors:Supathorn?Phongikaroon  author-information"  >  author-information__contact u-icon-before"  >  mailto:supathorn@nrl.navy.mil"   title="  supathorn@nrl.navy.mil"   itemprop="  email"   data-track="  click"   data-track-action="  Email author"   data-track-label="  "  >Email author,Richard?V.?Calabrese,Keith?Carpenter
Affiliation:(1) Dept. of Chemical Engineering, University of Maryland, 20742 College Park, MD;(2) Institute of Chemical and Engineering Sciences, Pesek Rd., 627833 Jurong Island, Singapore;(3) Present address: Remote Sensing Division, Naval Research Laboratory, 20375 Washington, D.C.
Abstract:In this study, the effect of high energy input from mechanical agitation, provided with a high shear rotor-stator, on the drop size and the drop size distribution (DSD) of aqueous polyurethane (PU) dispersions is investigated. The effect of the dispersed phase volume fraction (ϕ) on the DSD of aqueous PU dispersions is also examined to understand the fundamental characteristics that result from the high shear mixing. DSD is measured by using either a high magnification video probe or dynamic light scattering, depending on the range of drop sizes. For the PU without any ionic content, the distributions appear to be bimodal with rather large drop sizes. The mean sizes of the first and second modes are about 10 and 22 μm, respectively. For the PU with an ionic content, the mean drop sizes are approximately 80 nm. The distributions reveal that functional chemistry plays a more dominant role in the process of making PU dispersions than the mechanical agitation, and that ϕ has a weak effect on the mean drop sizes. The results further suggest that mechanical agitation can be used to control the breadth of the distributions.
Keywords:Isocyanates  latexes  colloids  emulsions  polyurethanes  waterborne  application characteristics  data analysis  statistics  urethane  dispersion  batch rotor-stator mixers  drop size distribution
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