Vincent Bernemann, M.Sc.


Eißendorfer Str. 38

Building O, Room 1.015

21073 Hamburg

Phone +49 40 42878 - 2603

Mail Vincent Bernemann


Biography

Vincent Bernemann completed his apprenticeship as a plant mechanic at Evonik Industries AG from 2011 to 2015. At the same time, he completed a degree in Industrial Service Management at the University of Applied Sciences Dortmund.

From 2015, he deepened his training by studying process engineering at the Technical University of Hamburg, initially in the bachelor's program and from 2019 in the master's program. Since graduating in 2021, he is employed as a research assistant at the Institute for Multiphase Flows.

Research

As part of the multiphase bioreactor research group, Vincent Bernemann investigates single-use bioreactors in various scales from 250 mL to 2000 L. In collaboration with Sartorius Stedim GmbH, the reactors are characterized and optimized experimentally with respect to various process parameters such as mass transfer, bubble size distribution, energy input and mixing time.

Education
  • Fundamentals of Material Engineering

Publications

[191132]
Title: Characterization Data for the Establishment of Scale-Up and Process Transfer Strategies between Stainless Steel and Single-Use Bioreactors.
Written by: Bernemann, V.; Fitschen, J.; Leupold, M.; Scheibenbogen, K.-H.; Maly, M.; Hoffmann, M.; Wucherpfennig, T.; Schlüter, M.
in: <em>Fluids</em>. (2024).
Volume: <strong>9</strong>. Number: (5),
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DOI: 10.3390/fluids9050115
URL: https://www.mdpi.com/2311-5521/9/5/115
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Abstract: The reliable transfer of bioprocesses from single-use bioreactors (SUBs) of different scales to conventional stainless steel stirred-tank bioreactors is of steadily growing interest. In this publication, a scale-up study for SUBs with volumes of 200 L and 2000 L and the transfer to an industrial-scale conventional stainless steel stirred-tank bioreactor with a volume of 15,000 L is presented. The scale-up and transfer are based on a comparison of mixing times and the modeling of volumetric mass transfer coefficients kLa, measured in all three reactors in aqueous PBS/Kolliphor solution. The mass transfer coefficients are compared with the widely used correlation of van’t Riet at constant stirrer tip speeds. It can be shown that a van’t Riet correlation enables a robust and reliable prediction of mass transfer coefficients on each scale for a wide range of stirrer tip speeds and aeration rates. The process transfer from single-use bioreactors to conventional stainless steel stirred-tank bioreactors is proven to be uncritical concerning mass transfer performance. This provides higher flexibility with respect to bioreactor equipment considered for specific processes.