Juraeva Makhsuda, Kang Dong Jin
School of mechanical engineering, Yeungnam University, Gyungsan 712-749, Korea.
Micromachines (Basel). 2020 Jul 15;11(7):685. doi: 10.3390/mi11070685.
A new cross-channel split-and-recombine (CC-SAR) micro-mixer was proposed, and its performance was demonstrated numerically. A numerical study was carried out over a wide range of volume flow rates from 3.1 μL/min to 826.8 μL/min. The corresponding Reynolds number ranges from 0.3 to 80. The present micro-mixer consists of four mixing units. Each mixing unit is constructed by combining one split-and-recombine (SAR) unit with a mixing cell. The mixing performance was analyzed in terms of the degree of mixing and relative mixing cost. All numerical results show that the present micro-mixer performs better than other micro-mixers based on SARs over a wide range of volume flow rate. The mixing enhancement is realized by a particular motion of vortex flow: the Dean vortex in the circular sub-channel and another vortex inside the mixing cell. The two vortex flows are generated on the different planes perpendicular to each other. They cause the two fluids to change their relative position as the fluids flow into the circular sub-channel of the SAR, eventually promoting violent mixing. High vorticity in the mixing cell elongates the flow interface between two fluids, and promotes mixing in the flow regime of molecular diffusion dominance.
提出了一种新型的跨通道分裂与重组(CC-SAR)微混合器,并对其性能进行了数值验证。在3.1 μL/min至826.8 μL/min的宽体积流量范围内进行了数值研究。相应的雷诺数范围为0.3至80。当前的微混合器由四个混合单元组成。每个混合单元通过将一个分裂与重组(SAR)单元与一个混合池相结合来构建。从混合程度和相对混合成本方面分析了混合性能。所有数值结果表明,在宽体积流量范围内,当前的微混合器比基于SAR的其他微混合器性能更好。混合增强是通过一种特殊的涡流运动实现的:圆形子通道中的迪恩涡和混合池内的另一个涡。这两种涡流在相互垂直的不同平面上产生。当流体流入SAR的圆形子通道时,它们使两种流体改变其相对位置,最终促进剧烈混合。混合池中的高涡度拉长了两种流体之间的流动界面,并在分子扩散主导的流动状态下促进混合。