Drop breakup inviscous liquids in agitated vessels occurs in elongational flow around impeller blade edges. The drop size distributions measured over extended periods for impellers of different sizes show that breakup process continues up to 15-20 h, before a steady state is reached. The size distributions evolve in a self-similar way till the steady state is reached. The scaled size distributions vary with impeller size and impeller speed, in contrast with the near universal scaling known for drop breakup in turbulent flows. The steady state size of the largest drop follows inverse scaling with impeller tip velocity. The breadth of the scaled size distributions also shows a monotonic relationship with impeller tip velocity only. (C) 2011 E...
Emulsion formation is of great interest in the chemical and food industry and droplet breakup is the...
The problem of breakup and coalescence of droplets in fully turbulent Couette flow is investigated t...
We investigate the stretching and breakup of a drop freely suspended in a viscous fluid undergoing c...
A detailed experimental and simulation study has been carried out in the present work to understand ...
Kumar el al. (1991, Chem. Engng Sci. 46, 2483-2489) have shown that in a stirred vessel, size of the...
Agitation of two immiscible liquids or solid-liquid suspension is a frequent operation in chemical a...
We report a study on the deformation and breakup of drops in an impulsively started shear flow under...
Two-liquid phase dispersion in mechanically stirred vessels is a key step in many operations in the ...
The extent to which dispersed-phase viscosity influences equilibrium mean drop size and drop size di...
An experimental study of the primary breakup in the near-injector region of large diameter (3.6-9.5 ...
Two phase liquid dispersions are used in many engineering operations such as liquid-liquid extractio...
International audienceThe study of phase dispersion of two immiscible fluids in different flows requ...
Mixing of immiscible liquid-liquid system is the crucial process for many branches of industry. The ...
The relative influence of dispersed-phase viscosity and interfacial tension on equilibrium drop size...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
Emulsion formation is of great interest in the chemical and food industry and droplet breakup is the...
The problem of breakup and coalescence of droplets in fully turbulent Couette flow is investigated t...
We investigate the stretching and breakup of a drop freely suspended in a viscous fluid undergoing c...
A detailed experimental and simulation study has been carried out in the present work to understand ...
Kumar el al. (1991, Chem. Engng Sci. 46, 2483-2489) have shown that in a stirred vessel, size of the...
Agitation of two immiscible liquids or solid-liquid suspension is a frequent operation in chemical a...
We report a study on the deformation and breakup of drops in an impulsively started shear flow under...
Two-liquid phase dispersion in mechanically stirred vessels is a key step in many operations in the ...
The extent to which dispersed-phase viscosity influences equilibrium mean drop size and drop size di...
An experimental study of the primary breakup in the near-injector region of large diameter (3.6-9.5 ...
Two phase liquid dispersions are used in many engineering operations such as liquid-liquid extractio...
International audienceThe study of phase dispersion of two immiscible fluids in different flows requ...
Mixing of immiscible liquid-liquid system is the crucial process for many branches of industry. The ...
The relative influence of dispersed-phase viscosity and interfacial tension on equilibrium drop size...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
Emulsion formation is of great interest in the chemical and food industry and droplet breakup is the...
The problem of breakup and coalescence of droplets in fully turbulent Couette flow is investigated t...
We investigate the stretching and breakup of a drop freely suspended in a viscous fluid undergoing c...