2000
DOI: 10.1002/1099-0488(20010115)39:2<201::aid-polb20>3.0.co;2-o
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Continuous phase viscosity influence on maximum diameters of poly(styrene-divinylbenzene) beads prepared by suspension polymerization

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Cited by 10 publications
(5 citation statements)
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“…For the current study of the abnormal emulsions with PIB as the continuous phase, however, the viscosity of the emulsion is rather high, even for a low value of f d . There is some evidence that, with increasing viscosity of the continuous phase, the size of dispersed drops does not significantly vary, or may even be reduced. , It is speculated that, with a high continuous phase viscosity, the shear stress exerted on the dispersed water drops is sufficiently high to allow for an intensive drop deformation with subsequent inclusions. The internal oil droplets formed in the preinversion region are so small that they could not be further reduced under the high-intensity turbulence of the postinversion region and they maintain their identity in the postinversion structures when they are released to the continuous water phase.…”
Section: Resultsmentioning
confidence: 99%
“…For the current study of the abnormal emulsions with PIB as the continuous phase, however, the viscosity of the emulsion is rather high, even for a low value of f d . There is some evidence that, with increasing viscosity of the continuous phase, the size of dispersed drops does not significantly vary, or may even be reduced. , It is speculated that, with a high continuous phase viscosity, the shear stress exerted on the dispersed water drops is sufficiently high to allow for an intensive drop deformation with subsequent inclusions. The internal oil droplets formed in the preinversion region are so small that they could not be further reduced under the high-intensity turbulence of the postinversion region and they maintain their identity in the postinversion structures when they are released to the continuous water phase.…”
Section: Resultsmentioning
confidence: 99%
“…This is also indicated by the values of the Taylor number (Jegat et al, 2001). These indications have to be verified by the experimental data which must be consistent with the prevailing mechanism.…”
Section: Determination Of the Dispersion Mechanismmentioning
confidence: 99%
“…When viscosity-increasing agents were present in the continuous phase for the suspension copolymerization of styrene and divinylbenzene, Jegat et al [41] found that drop breakage could occur via viscous shear when flow in the suspension was turbulent. In that case, the Kolmogorov length would have been larger that that found when low-viscosity aqueous solutions are used.…”
Section: Drop Breakage Mechanismsmentioning
confidence: 99%