In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity drops in turbulent flows by determining the dynamics of deformation of an inviscid drop in response to a pressure variation acting on the drop surface. Known scaling relationships between wavenumbers and frequencies, and between pressure fluctuations and velocity fluctuations in the inertial subrange are used in characterizing the pressure fluctuation. The existence of a maximum stable drop diameter d(max) follows once scaling laws of turbulent flow are used to correlate the magnitude of the disruptive forces with the duration for which they act. Two undetermined dimensionless quantities, both of order unity, appear in the equations of contin...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
The value of the average drop size in a stirred liquid-liquid dispersion is required for the analysi...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
The deformation of a drop (or bubble) in a turbulent flow combines two complex physical mechanisms: ...
A model of breakage of drops in a stirred vessel has been proposed to account for the effect of rheo...
This paper deals with drop and bubble break-up modelling in turbulent flows. We consider the case wh...
International audienceThis paper deals with drop and bubble break-up modelling in turbulent flows. W...
This paper deals with drop and bubble break-up modelling in turbulent flows. We consider the case wh...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
The value of the average drop size in a stirred liquid-liquid dispersion is required for the analysi...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
In this work, an attempt is made to gain a better understanding of the breakage of low-viscosity dro...
The deformation of a drop (or bubble) in a turbulent flow combines two complex physical mechanisms: ...
A model of breakage of drops in a stirred vessel has been proposed to account for the effect of rheo...
This paper deals with drop and bubble break-up modelling in turbulent flows. We consider the case wh...
International audienceThis paper deals with drop and bubble break-up modelling in turbulent flows. W...
This paper deals with drop and bubble break-up modelling in turbulent flows. We consider the case wh...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
The existing models of drop breakage in stirred turbulent dispersions are applicable only to purely ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
Existing models for dmax predict that, in the limit of μd → ∞, dmax increases with 3/4 power of μd. ...
The value of the average drop size in a stirred liquid-liquid dispersion is required for the analysi...