Analysis of a microreactor for synthesizing nanocrystals by computational fluid dynamics

Microreactors eliminate batch‐to‐batch variability and allow better control over nanocrystal synthesis. A serpentine microreactor fabricated by femtosecond laser ablation is presented and characterized by computational fluid dynamics, since the micro channels show a trapezoidal cross‐section mainly...

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Veröffentlicht in:Canadian journal of chemical engineering 2019-02, Vol.97 (2), p.594-603
Hauptverfasser: Peres, José Carlos Gonçalves, Herrera, Cristhiano da Costa, Baldochi, Sonia Licia, de Rossi, Wagner, dos Santos Vianna, Ardson
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container_issue 2
container_start_page 594
container_title Canadian journal of chemical engineering
container_volume 97
creator Peres, José Carlos Gonçalves
Herrera, Cristhiano da Costa
Baldochi, Sonia Licia
de Rossi, Wagner
dos Santos Vianna, Ardson
description Microreactors eliminate batch‐to‐batch variability and allow better control over nanocrystal synthesis. A serpentine microreactor fabricated by femtosecond laser ablation is presented and characterized by computational fluid dynamics, since the micro channels show a trapezoidal cross‐section mainly due to the relatively high numerical aperture of the focusing lens. Mixing, macro and micro, throughout the device was investigated for inlet flow rates between 10–500 μL min−1 and the injection of an inert tracer with the same transport properties of water. The simulation of the whole microreactor enabled the analysis of the formation and destruction of structures. For instance, secondary flows played a major role in mixing behaviour: small flow rates did not promote mixing of the tracer and a stream of pure water even after 43 curved segments, while they were perfectly mixed after 9 segments for higher flow rates. According to the mixing index, the maximum effect of convective mixing was achieved for an inlet flow rate of 250 μL min−1. Tracer dispersion and the mixing index guided a scale‐up process of the microreactor, optimizing the number of curved segments while increasing total throughput. The upscaled design exhibited mixing saturation at 400 μL min−1 and promoted better control of residence time to allow nanocrystal growth. Dynamics of secondary flows at the mixing section curved segments for flow rate 250 μL min−1.
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Tracer dispersion and the mixing index guided a scale‐up process of the microreactor, optimizing the number of curved segments while increasing total throughput. The upscaled design exhibited mixing saturation at 400 μL min−1 and promoted better control of residence time to allow nanocrystal growth. 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subjects Computational fluid dynamics
Computer simulation
Flow velocity
Fluid dynamics
Inlet flow
laminar flow
Laser ablation
Microreactors
mixing
Nanocrystals
Numerical aperture
scale‐up
Segments
Serpentine
simulation
title Analysis of a microreactor for synthesizing nanocrystals by computational fluid dynamics
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