Abstract
The efficient blending and mixing of liquids are very important in most industrial technologies. Mixing is often carried out in tanks, reactors, or mixing apparatuses. Impellers are widely used in many industrial processes ranging from mining through hydrometallurgy to complex processes based on chemical reactions (e.g. fermentation, wastewater treatment, polymerization, crystallization). Mixing can be created in mechanical way by rotary elements on a shaft, or in pneumatically way by high-speed fluid flow. The quality of mixing has huge affect on the rate of transport processes (energy and/or mass) and on the reaction rate too in a chemical reactor. The mixing also contributes to the evaluation of the effects of the optimal operating parameters.
The required power and the flow pattern in a vessel depend on the impeller geometry. In the literature, there are only recommendation and no indices to help choosing an impeller for a defined mixing task. And that is not possible to optimize the revolution per minutes at mixing element that have the same design.
The primary goal of our research is to create a measure for quantitative characterization of the level of homogeneity in a stirred system resulted by different impeller geometries and rotating speed, and to compare the power consumptions.
