Mechanically agitated reactors with single and multiple impeller systems are used in the industry for the various three-phase mixing processes such as crystallization, fermentation, and hydrogenation, etc. The paper reviews the experimental work reported in the literature along with different techniques used for the measurement of the specific quantities such as minimum or critical impeller speed for solid suspension. The work critically surveys the literature and makes specific recommendations for the use of appropriate correlations and conditions to be used for the success of such equipment. This assessment will put all the relevant literature on a common footing and will help to validate work reported earlier
Liquid-liquid mixing is a key process in industries that is commonly accomplished in mechanical agit...
Nuclear criticality safety in Separations canyon facilities is maintained primarily by control of th...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
In this work, simulations have been performed for three phase stirred dispersions using computationa...
A mathematical model has been developed for describing the solid suspension on the basis of a sedime...
In this work, suspension of ultrahigh concentration solids in the presence of gas at different solid...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
Stirred tanks are widely used in chemical process industries for catalytic reactions, dissolution of...
Stirred tanks are widely used in chemical process industries for catalytic reactions, dissolution of...
A low-shear stirred vessel was explored. Experimental studies on the suspension of solid particles i...
Knowledge of particle-liquid mass transfer coefficient (k<SUB>SL</SUB>) is important for a rational ...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
Mechanically agitated vessels are used widely for gas-liquid-solid mixing operations in processing p...
Solid-liquid mixing vessels are employed widely in mineral processing industry for carrying out oper...
The hydrodynamic, heat and mass transfer characteristics of mechanically agitated contactors have be...
Liquid-liquid mixing is a key process in industries that is commonly accomplished in mechanical agit...
Nuclear criticality safety in Separations canyon facilities is maintained primarily by control of th...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...
In this work, simulations have been performed for three phase stirred dispersions using computationa...
A mathematical model has been developed for describing the solid suspension on the basis of a sedime...
In this work, suspension of ultrahigh concentration solids in the presence of gas at different solid...
Liquid phase mixing time (θmix) was measured in mechanically agitated contactors of internal diamete...
Stirred tanks are widely used in chemical process industries for catalytic reactions, dissolution of...
Stirred tanks are widely used in chemical process industries for catalytic reactions, dissolution of...
A low-shear stirred vessel was explored. Experimental studies on the suspension of solid particles i...
Knowledge of particle-liquid mass transfer coefficient (k<SUB>SL</SUB>) is important for a rational ...
Liquid phase mixing and power consumption have been studied in 0.3, 0.57, 1.0 and 1.5 m i.d. mechani...
Mechanically agitated vessels are used widely for gas-liquid-solid mixing operations in processing p...
Solid-liquid mixing vessels are employed widely in mineral processing industry for carrying out oper...
The hydrodynamic, heat and mass transfer characteristics of mechanically agitated contactors have be...
Liquid-liquid mixing is a key process in industries that is commonly accomplished in mechanical agit...
Nuclear criticality safety in Separations canyon facilities is maintained primarily by control of th...
Liquid-phase mixing has been studied in mechanically agitated contactors of internal diameter 0.57 m...