Experimental study of efficient mixing in a micro-fluidized bed

被引:8
作者
Zivkovic, Vladimir [1 ]
Ridge, Nadia [2 ]
Biggs, Mark J. [2 ,3 ]
机构
[1] Newcastle Univ, Sch Engn, Newcastle NE1 7RU, England
[2] Univ Adelaide, Sch Chem Engn, Adelaide, SA 5005, Australia
[3] Loughborough Univ Technol, Sch Sci, Loughborough LE11 3TU, Leics, England
关键词
Fluidization; Mixing efficiency; Micro-fluidized bed; Micro-mixer; Multiphase flow; Process intensification; ON-A-CHIP; TOTAL ANALYSIS SYSTEMS; SPHERICAL-PARTICLES; HEAT-EXCHANGERS; PACKED BEDS; MICROFLUIDICS; MICROMIXERS; FLOW; QUANTIFICATION; RECONSTRUCTION;
D O I
10.1016/j.applthermaleng.2017.08.144
中图分类号
O414.1 [热力学];
学科分类号
摘要
Micro-fluidized beds represent a novel means of significantly enhancing mixing and mass and heat transfer under the low Reynolds number flows that dominate in microfluidic devices. This study experimentally evaluates the mixing performance of a micro-fluidized bed and the improvements it affords over the equivalent particle-free system. The dye dilution technique coupled with standard top-view image analysis was used to characterize the mixing in a 400 x 175 mu m(2) polydimethylsiloxane (PDMS) Y-microchannel. Overall, the micro-fluidized bed provided a mixing effectiveness and energetic efficiency of mixing that were up to three times greater than those of a particle-free channel of the same dimensions. The mixing performance is strongly affected by specific power input and bed voidage. The optimal operating voidage, which corresponds to the energetic efficiency of mixing being maximal, is around 0.77 for the smallest particle-to-channel size ratio considered here 0.121, and appears to increase beyond this with size ratio. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1642 / 1649
页数:8
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