The mechanical power consumed in agitating aerated and nonaerated aqueous phases was measured and correlated using the data of previous investigators. The correlation is for a flat bladed turbine operating within the turbulent regime in fully baffled vessels. The accuracy of the predictions and the range of geometrical variations and equipment sizes support the use of the correlation for scaleup opreations. Copyright © 1982 American Institute of Chemical Engineer
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...
A significant amount of data can be found in the literature on power consumption of single-impeller ...
Experiments are carried out in a baffled flat-bottom stirred tank to test live dual-impeller configu...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
The mixing pattern and power number in a stirred vessel depend not only on the impeller design but a...
The paper presents an analysis of power consumption in mixing and dispersing of air into a shear thi...
Flow induced by a dual turbine stirred tank was characterized measuring local velocities with a LDV ...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
The effect on the mixing time of the density difference between the tracer fluid and the bulk, the t...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
The power consumed by one, two, or three downward pumping, 45 degrees six-blade pitched-blade turbin...
Two-phase turbines open the possibility of new types of power cycles operating with extremely wet mi...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...
A significant amount of data can be found in the literature on power consumption of single-impeller ...
Experiments are carried out in a baffled flat-bottom stirred tank to test live dual-impeller configu...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
The mixing pattern and power number in a stirred vessel depend not only on the impeller design but a...
The paper presents an analysis of power consumption in mixing and dispersing of air into a shear thi...
Flow induced by a dual turbine stirred tank was characterized measuring local velocities with a LDV ...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
The effect on the mixing time of the density difference between the tracer fluid and the bulk, the t...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
The power consumed by one, two, or three downward pumping, 45 degrees six-blade pitched-blade turbin...
Two-phase turbines open the possibility of new types of power cycles operating with extremely wet mi...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...