In this study, agitation of solutions using different impeller and tank geometry were investigated experimentally in terms of hydrodynamics, macromixing time and aeration characteristics. In the first set of experiments a cylindrical vessel equipped with two types of hydrofoil and a hyperboloid impeller or their combinations were used. Vessel and impeller diameters and water level were 300, 100 and 300 mm, respectively. At the same specific power consumption, 163 W/m3, the so called “hydrofoil 1” impeller provided the shortest mixing time at 7.8 s. At the top hydrofoil 1 impeller submergence of 100 mm, the hyperboloid impeller combination of it was the most efficient by a mixing time of 10.0 s at 163 W/m3. Ultrasound Doppler velocimetry and...
Mixing phenomena are regarded as one of the major factors responsible for the failure to successfull...
Mixing characteristics of liquid phase in an unbaffled vessel containing water with a liquid height-...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Current literature relies almost...
A flow and mixing model can provide a sound fundamental basis for the quantitative and optimum desig...
In this paper, the experimental data on the mixing time ad power consumption of two immiscible liqui...
A theoretical study on the hydrodynamics of mixing processes in stirred tanks is described. The prim...
Impeller submergence governs the performance of mixing tanks employed in oxygen transfer operation. ...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
This study was conducted to investigate the effects of impeller blade geometry/inclination on mixing...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
The flow pattern and power number in a vessel depend on the impeller blade angle, number of blades, ...
Mixing phenomena are regarded as one of the major factors responsible for the failure to successfull...
Mixing characteristics of liquid phase in an unbaffled vessel containing water with a liquid height-...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Current literature relies almost...
A flow and mixing model can provide a sound fundamental basis for the quantitative and optimum desig...
In this paper, the experimental data on the mixing time ad power consumption of two immiscible liqui...
A theoretical study on the hydrodynamics of mixing processes in stirred tanks is described. The prim...
Impeller submergence governs the performance of mixing tanks employed in oxygen transfer operation. ...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
This study was conducted to investigate the effects of impeller blade geometry/inclination on mixing...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
The flow pattern and power number in a vessel depend on the impeller blade angle, number of blades, ...
Mixing phenomena are regarded as one of the major factors responsible for the failure to successfull...
Mixing characteristics of liquid phase in an unbaffled vessel containing water with a liquid height-...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...