The aim of the research presented in this paper was determination of power consumption and gas hold-up in mechanically agitated aerated aqueous low concentration sucrose solutions. Experimental studies were conducted in a vessel of diameter 0.634 m equipped with high-speed impellers (Rushton turbine, Smith turbine or A 315). The following operating parameters were changed: volumetric gas flow rate (expressed by superficial gas velocity), impeller speed, sucrose concentration and type of impeller. Based on the experiments results, impellers with a modified shape of blades, e.g. CD 6 or A 315, could be recommended for such gas-liquid systems. Power consumption was measured using strain gauge method. The results of gas holdup measurements have...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...
The influence of impellers system, baffles system and type of liquid on gas hold-up in a vessel has ...
In some industrial processes there is the necessity of if exhausting a gaseous component in a liquid...
The aim of the research presented in this paper was to determine the effect of vessel scale on gas h...
The aim of the research presented in this paper was to determine the effect of vessel scale on gas h...
The paper presents an analysis of power consumption in mixing and dispersing of air into a shear thi...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
Power consumption was measured in 0.57, 1.0, and 1.5 m i.d. gas inducing type of mechanically agitat...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The steady state mass transfer coefficient, k(L)a, and the hold-up, epsilon, have been measured in a...
In a vessel with inner diameter 0.29 m supplied by one, two or three impellers on a common shaft, th...
The steady state mass transfer coefficient, k(L)a, and the hold-up, epsilon, have been measured in a...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...
The influence of impellers system, baffles system and type of liquid on gas hold-up in a vessel has ...
In some industrial processes there is the necessity of if exhausting a gaseous component in a liquid...
The aim of the research presented in this paper was to determine the effect of vessel scale on gas h...
The aim of the research presented in this paper was to determine the effect of vessel scale on gas h...
The paper presents an analysis of power consumption in mixing and dispersing of air into a shear thi...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
Power consumption was measured in 0.57, 1.0, and 1.5 m i.d. gas inducing type of mechanically agitat...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The aim of this work is to investigate the influence of the main geometrical and hydrodynamic charac...
The steady state mass transfer coefficient, k(L)a, and the hold-up, epsilon, have been measured in a...
In a vessel with inner diameter 0.29 m supplied by one, two or three impellers on a common shaft, th...
The steady state mass transfer coefficient, k(L)a, and the hold-up, epsilon, have been measured in a...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
Abstract. Measurements of the power consumption and the determination of the minimum speed and power...
The influence of impellers system, baffles system and type of liquid on gas hold-up in a vessel has ...
In some industrial processes there is the necessity of if exhausting a gaseous component in a liquid...