AbstractIn this article, the data assembled regarding the mixing of Newtonian and shear thinning fluids by screw impellers in a cylindrical tank is disclosed. The data summarizing some information on the efficiency of such impellers are obtained via 3D calculations of velocities and viscous dissipation in the whole vessel volume. The data presented herein may be useful for those who want to outline the mixing characteristics in terms of fluid circulation and power consumption for this kind of impellers, therefore, avoiding a great effort for achieving a high number of experiments
The effect of multiple Intermig impeller configuration on hydrodynamics and mixing performance in a ...
ABSTRACT: The vast majority of solid–liquid mixing studies have focused on high Reynolds number appl...
AbstractThe mixing of ideal viscoelastic (Boger) fluids within a Kenics KM static mixer has been ass...
In this article, the data assembled regarding the mixing of Newtonian and shear thinning fluids by s...
AbstractThe mixing of high viscosity and viscoelastic fluids may be performed in industry using a “b...
The present paper deals with the mixing of a highly viscous fluid by close-clearance impellers in cy...
Mixing has the most common occurrence in process industries like chemical, food and polymer and play...
The fluid flows and power consumption in a vessel stirred by anchor impellers are investigated in th...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The impeller design is the most crucial parameter to enhance the performance of stirred tanks. The c...
Red. serii Monografie : Wodziński, PiotrBased on years of industrial experience and laboratory tests...
Mean and rms velocity characteristics of two Newtonian flows at Reynolds numbers of 12,800 (glycerin...
Blend times and power consumption have been measured for Newtonian and pseudo- plastic fluids in ag...
Mixing viscoelastic fluids is common to many chemical and biochemical process industries where the r...
The present study investigates experimentally the laminar mixing and heat transfer of a range of he...
The effect of multiple Intermig impeller configuration on hydrodynamics and mixing performance in a ...
ABSTRACT: The vast majority of solid–liquid mixing studies have focused on high Reynolds number appl...
AbstractThe mixing of ideal viscoelastic (Boger) fluids within a Kenics KM static mixer has been ass...
In this article, the data assembled regarding the mixing of Newtonian and shear thinning fluids by s...
AbstractThe mixing of high viscosity and viscoelastic fluids may be performed in industry using a “b...
The present paper deals with the mixing of a highly viscous fluid by close-clearance impellers in cy...
Mixing has the most common occurrence in process industries like chemical, food and polymer and play...
The fluid flows and power consumption in a vessel stirred by anchor impellers are investigated in th...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The impeller design is the most crucial parameter to enhance the performance of stirred tanks. The c...
Red. serii Monografie : Wodziński, PiotrBased on years of industrial experience and laboratory tests...
Mean and rms velocity characteristics of two Newtonian flows at Reynolds numbers of 12,800 (glycerin...
Blend times and power consumption have been measured for Newtonian and pseudo- plastic fluids in ag...
Mixing viscoelastic fluids is common to many chemical and biochemical process industries where the r...
The present study investigates experimentally the laminar mixing and heat transfer of a range of he...
The effect of multiple Intermig impeller configuration on hydrodynamics and mixing performance in a ...
ABSTRACT: The vast majority of solid–liquid mixing studies have focused on high Reynolds number appl...
AbstractThe mixing of ideal viscoelastic (Boger) fluids within a Kenics KM static mixer has been ass...