Abstract

Stirred tank reactors are frequently used for mixing as well as heat- and mass transfer processes in chemical and biochemical engineering due to their robust operation and extensive experiences in the past. However, for cell culture processes like mammalian cell expression systems, special requirements have to be met to ensure optimal cell growth and product quality. One of the most important requirements to ensure ideal transport processes is a proper mixing performance, characterized typically by the global mixing time tmix,global or the dimensionless global mixing time tmix,global·n. As an evaluation method for mixing time determination, the time is usually determined until a tracer signal (e.g. conductivity) has reached a constant value after a peak has been introduced (e.g. by adding a salt). A disadvantage of this method is, that the position of tracer feeding as well as the position of the probe significantly influences the detected mixing time. Further on, the global mixing time does not provide any information about the spatial and temporal ”history” of the mixing process to identify areas that are mixed poorly or areas that form stable compartments. To overcome this disadvantage, a novel image analysis will be presented in this study for the detailed characterization of mixing processes by taking into account the history of mixing. The method is based on the experimental determination of the local mixing time distribution by using a multi-color change caused by a pH-change in a bromothymol blue solution. A 3L transparent stirred tank reactor is used for the benchmark experiment. To demonstrate the suitability of the new characterization method for the validation of numerical simulations, a calculation with a commercial Lattice-Boltzmann approach (M-Star CFD) has been performed additionally and evaluated regarding mixing time distributions. The exemplary application of image analysis to a numerical mixing time simulation shows good agreement with the corresponding experiment. On the one hand, this shows that the method can also be interesting for numerical work, especially for experimental validation, and on the other hand, this allows much deeper insights into the mixing behavior compared to conventional mixing criteria. For example the new method enables the characterization of mixing on different scales as well as the identification of micro- and macroscopic flow structures. The strong influence of the acid to base ratio on mixing time experiments becomes clearly visible with the new method.

Highlights

  • In chemical and bioprocess engineering, mixing plays a key role, since it controls the process performance regarding solid suspension, homogenization, dispersion of multiple phases, heat transfer and chemical reactions

  • The new measuring and visualization procedure is discussed in the following on the basis of the described 3 L stirred tank reactor for one stirrer speed and different acid to base ratios

  • The here presented experimental method for the visualization of the local mixing time distribution represents a new way for the process characterization and validation of numerical simulations

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Summary

Introduction

In chemical and bioprocess engineering, mixing plays a key role, since it controls the process performance regarding solid suspension, homogenization, dispersion of multiple phases, heat transfer and chemical reactions. A local and detailed insight regarding the mixing behavior in dead zones is especially important to detect phenomena like step wise compartment formation (Manikowski et al, 1994; Vasconcelos et al, 1996; Szalai et al, 2004; Sieblist et al, 2011; Woziwodzki and Jeßdrzejczak, 2011). This manuscript discusses a reliable method for a suitable determination of the local mixing degree of low viscous fluids in stirred tank reactors to determine the local mixing time. The application of the method to numerical simulations enables for the first time the experimental validation of numerical simulations, which is not limited to single instantaneous concentration distributions, but takes the temporal history of the mixing into account

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