739 research outputs found

    Fluchtmigration im Kontext von 20 Jahren Zuwanderung in die Stadt Freiburg

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    Hinter dem Wachstum der Stadt Freiburg in den letzten 20 Jahren verbergen sich insbesondere beim Zuzug aus dem Ausland vielfältige Migrationsformen, obwohl in der medialen und öffentlichen Wahrnehmung der letzten Jahre nur die Fluchtmigration präsent war. Die Zuwanderung lässt sich dabei nach der Herkunft klassifizieren oder nach Art der Migration. Hierbei kann unterschieden werden in Arbeitsmigration (Osteuropa), Bildungsmigration, Fluchtmigration und Mischmigration (Westeuropa). Es wird deutlich gemacht, dass für Freiburg die Arbeitsmigration und Bildungsmigration relevanter sind als die Fluchtmigration. In der kleinräumigen Verteilung zeigt sich, dass die Fluchtmigration am stärksten segregiert und die Mischmigration annähernd gleichverteilt ist

    The Cytokinin Status of the Epidermis Regulates Aspects of Vegetative and Reproductive Development in Arabidopsis thaliana

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    The epidermal cell layer of plants has important functions in regulating plant growth and development. We have studied the impact of an altered epidermal cytokinin metabolism on Arabidopsis shoot development. Increased epidermal cytokinin synthesis or breakdown was achieved through expression of the cytokinin synthesis gene LOG4 and the cytokinin-degrading CKX1 gene, respectively, under the control of the epidermis-specific AtML1 promoter. During vegetative growth, increased epidermal cytokinin production caused an increased size of the shoot apical meristem and promoted earlier flowering. Leaves became larger and the shoots showed an earlier juvenile-to-adult transition. An increased cytokinin breakdown had the opposite effect on these phenotypic traits indicating that epidermal cytokinin metabolism can be a factor regulating these aspects of shoot development. The phenotypic consequences of abbreviated cytokinin signaling in the epidermis achieved through expression of the ARR1-SRDX repressor were generally milder or even absent indicating that the epidermal cytokinin acts, at least in part, cell non-autonomously. Enhanced epidermal cytokinin synthesis delayed cell differentiation during leaf development leading to an increased cell proliferation and leaf growth. Genetic analysis showed that this cytokinin activity was mediated mainly by the AHK3 receptor and the transcription factor ARR1. We also demonstrate that epidermal cytokinin promotes leaf growth in a largely cell-autonomous fashion. Increased cytokinin synthesis in the outer layer of reproductive tissues and in the placenta enhanced ovule formation by the placenta and caused the formation of larger siliques. This led to a higher number of seeds in larger pods resulting in an increased seed yield per plant. Collectively, the results provide evidence that the cytokinin metabolism in the epidermis is a relevant parameter determining vegetative and reproductive plant growth and development

    Nutzung von Sensor Spots zur Bestimmung der Gelöstsauerstoffkonzentration in Single-use Systemen im Labormassstab

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    Einleitung: Der wirtschaftlich gewinnbringende Einsatz biotechnologischer Verfahren setzt eine explizite Kenntnis des verwendeten Systems voraus. Für aerobe Kultivierungen bedeutet dies insbesondere die Überwachung und Optimierung der Gelöstsauerstoffkonzentration im Bioreaktor. Dies gilt sowohl für die zunehmend an Bedeutung gewinnenden Single-Use Systeme als auch für klassische Bioreaktoren, wobei sich für erstere durch ihre besonderen Eigenschaften Chancen und Herausforderungen ergeben. Einsatzgebiete: Der Einsatz klassischer Messsonden in Single-Use Systemen widerspricht dem zugrundeliegenden out of the box Konzept und erhöht gleichzeitig den Aufwand in Vorbereitung und das Risiko einer Kontamination. Für Systeme wie Schüttelkolben oder Bagreaktoren ist der Einsatz dieser Messsonden aus geometrischen und strömungstechnischen Gründen zudem wenig sinnvoll. In diesem Anwendungsfeld (Laborbioreaktoren im Milliliter- und Litermaßstab) bieten Sensor Spots eine einfache und vielversprechende Alternative zur Sauerstoffüberwachung. In der vorliegenden Posterpräsentation wird der Einsatz von Sensor Spots zur Bestimmung des volumenbe-zogenen Sauerstoffübergangskoeffizienten (kLa-Wert) in verschiedenen Systemen (beispielsweise in Thomson Optimum Growth™ Schüttelkolben oder TubeSpin® Bioreaktoren) illustriert. Im Fokus steht dabei die Optimierung der Prozessparameter für pflanzliche und tierische Zellkulturen. Anwendungsbeispiele: Den Abschluss dieser Posterpräsentation bildet die Vorstellung verschiedener Auswertungsmöglichkeiten sowie die Demonstration der Einsatzmöglichkeiten unter verschiedenen Gesichtspunkten. Die Anwendung wird am Beispiel einer Kultivierungsstudie für CHO (Chinese Hamster Ovary) Zellen demonstriert

    Recommendations for the engineering characterization of single-use bioreactors

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    Single-use bioreactors have been available for more than 15 years and are nowadays widely accepted for a broad range of applications. However, process engineering data for these bioreactors, including volumetric mass transfer coefficients, mixing times and power inputs, are still limited. Furthermore, these data are often generated using a number of different methods, making comparisons difficult. In addition, the large variety of bioreactor types and their mixing principles (stirred, wave-mixed, orbitally-shaken, etc.) increases the difficulty in comparing the engineering data. In order to facilitate the usage of single-use bioreactors, the DECHEMA Upstream Processing (USP) expert group on ‘Single-use technology in biopharmaceutical manufacturing’ has developed recommendations for the process engineering characterization of single-use bioreactors. The methods are based on procedures that were previously developed for multi-use bioreactors and were tested in universities as well as companies (both from the supplier and user sides) for their robustness. The validated recommendations now include measurements of volumetric mass transfer coefficient, mixing time and power input. These parameters are experimentally determined using the dynamic gassing-out method, the decolorization method or sensor method, and the torque method respectively. The poster gives an overview of the fundamentals and procedures of the methods applied, and current results from the interlaboratory tests. Recent foci include the measurement of carbon dioxide gas-liquid mass transfer and the determination of mechanical stress due to hydrodynamics

    CFD for stirred bioreactors : analysis of different multiphase models to determine oxygen mass transfer

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    Oxygen supply of cells has a significant influence on cell growth and product yield. For this reason, biopharmaceutical manufacturers and their bioreactor suppliers are interested in optimizing the oxygen supply. In this context, computational fluid dynamics (CFD) can be used to calculate the kLa value in stirred bioreactors. First investigations have shown that both the volume-of-fluid (VOF) model and the compressible VOF model are unsuitable for the calculation of kLa values due to their lack of accuracy. Simulations with the Euler-Euler model showed significantly better agreement with experimental data, but the calculated kLa values were still about 50% higher than in the experiments. One reason could be the missing consideration of gas bubble breakup and coalescence. Therefore, various investigations were carried out with a population balance model (PBM)-coupled Euler-Euler model, which all were in better agreement with the experimental data, compared to the Euler-Euler model. With the help of the successfully established PBM-coupled CFD model it is now possible to calculate the oxygen mass transfer for stirred bioreactors. Thus, bioreactor and process design can be accomplished before prototyping, and time-consuming as well as cost-intensive laboratory experiments can be reduced. In order to verify the generality for all sizes of bioreactors, further validation work will be carried out

    Cultivation of CHO Cells in Thomson Optimum Growth™ Shake Flasks and Scale-up

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    In biotechnology, the usage of shaking flasks in upstream processing is widely common due to the easy handling. Frequent applications are process screening and optimization. Thereby, the focus lies mostly on a homogeneous and fast distribution of substrates and gases whilst power consumption and shearing force are meant to be kept low, which ideally results in high biomass concentrations and product titers. For characterization purposes, the mixing time and the oxygen mass transfer coefficient (kLa) were measured in 5 L and 500 mL Thomson Optimal Growth™ shaking flasks, using the de-colorization or the dynamic gassing-out method, respectively. Those geometrical optimized bioreactors are promising higher space-time yields compared to the predominant Erlenmeyer-shake flask design. According to the results of the procedural experiments, CHO (Chinese hamster ovary) cells were cultivated at selected, auspicious parameter combinations. The effectiveness of the predetermined parameters was evaluated and a scale-up method elaborated. The results can be summarized as follows: The key parameter for all experimental setups is the shaking rate. In contrast, the filling volume showed to have a more ambiguous role. Modeling results in the 500 mL flasks showed no significant influence of the filling volume to the maximal cell density, in contrast to the 5L flask (both shaken at 50 mm throw). The highest viable cell density (up to 4.8∙10⁶ cells mL⁻¹) was reached using the 500 mL flask with high shaking rates at 50 mm shaking diameter. Thereby, a µmax of 0.038 h-1 was achieved that correlates with a td of less than 19 h. All in all, the highest µmax of 0.055 h⁻¹ was reached during the scale-up process, whereby higher viable cell densities were reached compared to the batch cultivations using the same parameter settings. In addition to the experiments performed to date, simulations with computational fluid dynamics and experimental determination of specific power consumption rates are already in progress, increasing the range of applicability and the validity of the proposed model correlations

    Integration von Qualitätsdaten für Produktionsanlagen

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    In automatisierten Produktionsanlagen werden mehr und mehr Sensorsysteme eingesetzt, um die produzierte Qualität zu überwachen und auf Basis gesammelter Prozessdaten sicherzustellen. Die Heterogenität der an unterschiedlichen Stellen im Prozess integrierten Sensoren erfordert einen Ansatz zur einfachen Integration. Ziel der Integration ist die für verschiedene Rollen aufbereitete Qualitätssicht, die auch ein Feedback zur Fehlerdeduktion beinhaltet. In diesem Erfahrungsbericht wird der im Projekt BridgeIT entwickelte Ansatz zur syntaktischen und semantischen Integration von Qualitätsdaten vorgestellt. Der Ansatz ermöglicht insbesondere eine einfache Anbindung neuer Sensorsysteme
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