passive mixing
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Micromachines ◽  
2021 ◽  
Vol 12 (5) ◽  
pp. 556
Author(s):  
Ingrid. H. Oevreeide ◽  
Andreas Zoellner ◽  
Bjørn. T. Stokke

Functionalized sensor surfaces combined with microfluidic channels are becoming increasingly important in realizing efficient biosensing devices applicable to small sample volumes. Relaxing the limitations imposed by laminar flow of the microfluidic channels by passive mixing structures to enhance analyte mass transfer to the sensing area will further improve the performance of these devices. In this paper, we characterize the flow performance in a group of microfluidic flow channels with novel double curved passive mixing structures (DCMS) fabricated in the ceiling. The experimental strategy includes confocal imaging to monitor the stationary flow patterns downstream from the inlet where a fluorophore is included in one of the inlets in a Y-channel microfluidic device. Analyses of the fluorescence pattern projected both along the channel and transverse to the flow direction monitored details in the developing homogenization. The mixing index (MI) as a function of the channel length was found to be well accounted for by a double-exponential equilibration process, where the different parameters of the DCMS were found to affect the extent and length of the initial mixing component. The range of MI for a 1 cm channel length for the DCMS was 0.75–0.98, which is a range of MI comparable to micromixers with herringbone structures. Overall, this indicates that the DCMS is a high performing passive micromixer, but the sensitivity to geometric parameter values calls for the selection of certain values for the most efficient mixing.


Author(s):  
Long-Run Huang ◽  
Liang-Liang Fan ◽  
Qi Liu ◽  
Zhi Zhao ◽  
Jiang Zhe ◽  
...  
Keyword(s):  

Lab on a Chip ◽  
2021 ◽  
Vol 21 (20) ◽  
pp. 3910-3923
Author(s):  
Matteo Antognoli ◽  
Daniel Stoecklein ◽  
Chiara Galletti ◽  
Elisabetta Brunazzi ◽  
Dino Di Carlo

A fast method for designing optimal sequences of passive mixing units is provided for inertial flows. Intense mixing is achieved through highly-controlled stretching of the fluid contact surfaces.


RSC Advances ◽  
2021 ◽  
Vol 11 (41) ◽  
pp. 25677-25685
Author(s):  
Nurul Nadiah Hamidon ◽  
Gert IJ. Salentijn ◽  
Elisabeth Verpoorte

Efficient passive mixing can be achieved by contricting the reagent flow using structures having narrow gaps.


2020 ◽  
Vol 31 (1) ◽  
pp. 015006
Author(s):  
Ingrid H Oevreeide ◽  
Andreas Zoellner ◽  
Michal M Mielnik ◽  
Bjørn T Stokke

Nanomaterials ◽  
2020 ◽  
Vol 10 (11) ◽  
pp. 2202 ◽  
Author(s):  
Sahr Sana ◽  
Vladimir Zivkovic ◽  
Kamelia Boodhoo

Empirical correlations have been developed to relate experimentally determined starch nanoparticle size obtained in a solvent–antisolvent precipitation process with key hydrodynamic parameters of a spinning disc reactor (SDR). Three different combinations of dimensionless groups including a conventional Reynolds number (Re), rotational Reynolds number (Reω) and Rossby number (Ro) have been applied in individual models for two disc surfaces (smooth and grooved) to represent operating variables affecting film flow such as liquid flowrate and disc rotational speed, whilst initial supersaturation (S) has been included to represent varying antisolvent concentrations. Model 1 featuring a combination of Re, Reω and S shows good agreement with the experimental data for both the grooved and smooth discs. For the grooved disc, Re has a greater impact on particle size, whereas Reω is more influential on the smooth disc surface, the difference likely being due to the passive mixing induced by the grooves irrespective of the magnitude of the disc speed. Supersaturation has little impact on particle size within the limited initial supersaturation range studied. Model 2 which characterises both flow rate and disc rotational speed through Ro alone and combined with Re was less accurate in predicting particle size due to several inherent limitations.


Micromachines ◽  
2020 ◽  
Vol 11 (2) ◽  
pp. 175
Author(s):  
Su Deok Kim ◽  
Seo Woo Song ◽  
Dong Yoon Oh ◽  
Amos Chungwon Lee ◽  
Jeong Woo Koo ◽  
...  

The need for high-throughput screening has led to the miniaturization of the reaction volume of the chamber in bioassays. As the reactor gets smaller, surface tension dominates the gravitational or inertial force, and mixing efficiency decreases in small-scale reactions. Because passive mixing by simple diffusion in tens of microliter-scale volumes takes a long time, active mixing is needed. Here, we report an efficient micromixing method using magnetically rotating microparticles with patterned magnetization induced by magnetic nanoparticle chains. Because the microparticles have magnetization patterning due to fabrication with magnetic nanoparticle chains, the microparticles can rotate along the external rotating magnetic field, causing micromixing. We validated the reaction efficiency by comparing this micromixing method with other mixing methods such as simple diffusion and the use of a rocking shaker at various working volumes. This method has the potential to be widely utilized in suspension assay technology as an efficient mixing strategy.


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