2011
DOI: 10.1016/j.ces.2011.06.073
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Turbulent liquid–liquid dispersion in SMV static mixer at high dispersed phase concentration

Abstract: The aim of this paper is to investigate the influence of physico-chemical parameters on liquid-liquid dispersion at high dispersed phase concentration in Sulzer SMV TM mixer. Four different oil-in-water systems involving two different surfactants are used in order to evaluate the effect of interfacial tension, densities and viscosities ratio on mean droplets size diameters. Moreover the influence of the dispersed phase concentration on the pressure drop as well as on the droplet size distribution is investigat… Show more

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Cited by 49 publications
(52 citation statements)
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“…They dissipate energy continuously throughout the reactor's volume and generate a dispersion smaller in size than slugs [23][24][25]. The drawback of this approach is a generally greater pressure loss and/or lower residence time.…”
Section: Introductionmentioning
confidence: 99%
“…They dissipate energy continuously throughout the reactor's volume and generate a dispersion smaller in size than slugs [23][24][25]. The drawback of this approach is a generally greater pressure loss and/or lower residence time.…”
Section: Introductionmentioning
confidence: 99%
“…A remarkable feature of continuous liquid-liquid dispersion processes are their ability to create quickly droplet of controlled size. Whereas in batch stirred tank reactors, the emulsification time, defined as the time needed to reach stabilized mean droplets sizes, is typically about 15-30 min [17,[23][24][25][26], this time can be a limiting step when it comes to continuous process owning residence time ranging from microsecond, to millisecond, to second [15][16][17][18][19]. Table 1 provides some examples of mean droplet size correlation including their range of applications depending on the chemical parameters (viscosity, densities, and interfacial tension), equipment parameters (porosity, pore diameter, pipe diameter, stirrer dimension.…”
Section: Introductionmentioning
confidence: 99%
“…It has to be stable enough to prevent from coalescence and destabilization in course of polymerization. Different continuous processes are available to create liquid-liquid dispersion including membrane [13], rotor-stator [14], static mixer [15][16][17], colloid mills [14,18], high pressure homogenizer [19], mixer-settler [20] and pulsed column [21,22]. A remarkable feature of continuous liquid-liquid dispersion processes are their ability to create quickly droplet of controlled size.…”
Section: Introductionmentioning
confidence: 99%
“…5.4: A pulsating reactor from NiTech that provides a large gain in reaction volume [42]. 5.4: A pulsating reactor from NiTech that provides a large gain in reaction volume [42].…”
Section: Conductivity Probesmentioning
confidence: 99%