Hydrodynamics of gas/shear-thinning fluid flowing in a co-flow microchannel

IF 6.3 3区 工程技术 Q1 ENGINEERING, CHEMICAL Journal of the Taiwan Institute of Chemical Engineers Pub Date : 2025-06-01 Epub Date: 2025-03-03 DOI:10.1016/j.jtice.2025.106036
Wenyuan Fan , Shuaichao Li , Lixiang Li , Rujie Wang , Shiyang Liu , Taotao Fu
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Abstract

Background

Gas-liquid flow hydrodynamics are one of crucial roles in enhancing the interphase transport and reaction properties in microchannel reactors.

Methods

The hydrodynamics of gas-liquid flow in a co-flow microchannel with shear-thinning fluid were numerically investigated using a coupled level-set and volume-of-fluid method by considering the rheological characteristics of the fluid. The reliability of the numerical approach is validated through comparing the calculated liquid film thickness with film thickness in previous work quantitatively. The influences of liquid phase type, carboxymethylcellulose (CMC) solution and surfactant (SDS) concentrations on flow pattern and film thickness are elucidated respectively.

Significant findings

Five flow patterns, i.e., bubbly flow, Taylor flow, Taylor annular flow, annular flow, and churn flow, were intuitively identified in a broad range of liquid phases including water, CMC solution, and polyacrylamide (PAM) solution, and a fundamental flow pattern map has been constructed using the Weber numbers for two phases. The results indicate that the proportions occupied by bubbly flow and churn flow expand significantly whereas the areas associated with other patterns shrink in both non-Newtonian fluids compared to water. The similar transitions in flow pattern are enhanced overall by increasing CMC and SDS concentrations. The film thickness always increases linearly with capillary number in all fluids. The maximum film thickness exists in the most contaminated CMC solutions by SDS, whereas the minimum one in water. Finally, a novel scaling law of film thickness in a co-flow microchannel with shear-thinning liquids is developed and has satisfactory accuracy by comparing with the literature predictions.

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共流微通道中气体/剪切稀化流体的流体动力学
气液流体动力学是提高微通道反应器相间输运和反应性能的关键因素之一。方法在考虑流体流变特性的基础上,采用水平集和流体体积耦合的方法,对具有剪切稀化流体的共流微通道中气液流动的流体动力学进行了数值研究。通过将计算得到的液膜厚度与前人的液膜厚度进行定量比较,验证了数值方法的可靠性。研究了液相类型、羧甲基纤维素(CMC)溶液和表面活性剂(SDS)浓度对膜厚和流型的影响。在包括水、CMC溶液和聚丙烯酰胺(PAM)溶液在内的广泛的液相中,直观地识别出了气泡流、泰勒流、泰勒环流、环状流和搅拌流五种流动模式,并利用韦伯数构建了两相的基本流型图。结果表明,与水相比,两种非牛顿流体中气泡流和搅拌流所占的比例显著扩大,而与其他模式相关的区域则缩小。CMC和SDS浓度的增加总体上增强了流型的类似转变。在所有流体中,膜厚总是随毛细数线性增加。SDS污染最严重的CMC溶液中膜厚最大,水中膜厚最小。最后,建立了一种新的剪切减薄液体共流微通道膜厚的标度规律,并与文献预测结果进行了比较,得到了满意的精度。
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来源期刊
CiteScore
9.10
自引率
14.00%
发文量
362
审稿时长
35 days
期刊介绍: Journal of the Taiwan Institute of Chemical Engineers (formerly known as Journal of the Chinese Institute of Chemical Engineers) publishes original works, from fundamental principles to practical applications, in the broad field of chemical engineering with special focus on three aspects: Chemical and Biomolecular Science and Technology, Energy and Environmental Science and Technology, and Materials Science and Technology. Authors should choose for their manuscript an appropriate aspect section and a few related classifications when submitting to the journal online.
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