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International Conference on Magnetic Resonance Microscopy

Postersession - P-026

Flow-MRI of microfluidic reactors

S. Benders1*, M. Wiese2, S. Lehmkuhl1, E. Paciok1, M. Wessling2, 3, B. Blümich1
  • 1. RWTH Aachen University, Institut für Technische und Makromolekulare Chemie, Aachen, Germany
  • 2. RWTH Aachen University, Aachener Verfahrenstechnik, Aachen, Germany
  • 3. RWTH Aachen University, DWI - Leibniz-Institut für Interaktive Materialien e.V., Aachen, Germany

In conventional reactors the surface-to-volume ratio limits the capability of performing solid-state catalysis on the reactor walls. Overcoming this, microfluidic reactors offer several advantages over conventional reactors such as compact design. [1] To improve the reaction conditions it is crucial to analyse the flow within the reactor. This is done in this work by flow-MRI utilizing the flow-imaging employing single shot encoding (FLIESSEN) [2] and spin echo velocity imaging (SEVELIM) sequences.
The microfluidic reactor studied in this work has been 3D-printed with dimensions of 56 x 28 x 11 mm3 incorporating five channels (channel diameter approx. 0.848 mm). The channels are sealed with an exchangeable glass plate suitable for catalyst immobilization.

Get
Maps of the x- and z-velocities of the microfluidic reactor shot with FLIESSEN using segmentation and slice selection. The images are zero-filled by a factor of two and show (a) the x-component and (b) the z-component.

Velocity maps of water flowing through the reactor with 5 mL/h are shown in Figure 1. These were measured with the FLIESSEN sequence in an AV300 magnet with a Micro 2.5 gradient system with a maximum gradient strength of 1.57 T/m. The resolution is 130 x 90  μm2 with a Field-of-Flow of 20 mm/s and a slice thickness of 3 mm. The observed velocity distributions in the channels are shaped parabolic corresponding to laminar flow.
Get
z-velocity map of the microfluidic reactor measured with SEVELIM using slice selection in z-direction. The images are zero-filled by a factor of two.

In another orientation the velocity field in the channel cross section can be measured. The image was shot with the SEVELIM sequence with a slice selection of 7.5 mm (Figure 2). This figure shows the distorted half-circular shape of the channels along with the distribution of the z-velocities within them. The velocity is highest in the middle of the channel. Comparing the ratio of maximum and mean velocities within each channel leads to a ratio of 2.57 ± 0.12. The ratio is higher than the ratio of two for tubular flow in circular geometry. In summary, the presented microfluidic reactor shows distorted laminar flow.


  • [1]  J. Kobayashi, Y. Mori, K. Okamoto, R. Akiyama, M. Ueno, T. Kitamori, S. Kobayashi, (2004), A microfluidic device for conducting gas-liquid-solid hydrogenation reactions, Science, 1305-1308, 304 (5675)
  • [2]  A. Amar, B. Blümich, F. Casanova, (2010), Rapid multiphase flow dynamics mapped by single-shot mri velocimetry, ChemPhysChem, 2630-2638, (11)
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