粘弹性
气泡
微通道
机械
物理
流变学
粘度
两相流
流量(数学)
液体气泡
明渠流量
压力降
微流控
放松(心理学)
段塞流
流体力学
非牛顿流体
压力梯度
热力学
计算流体力学
流动可视化
流体体积法
下降(电信)
复杂流体
经典力学
最大气泡压力法
牛顿流体
起泡点
计算机模拟
颗粒流
体积流量
作者
Wei Zhang,Shaobai Li,Dang, Kang,Caixia Li,Yuhuan Ding,Wei Zhang,Shaobai Li,Dang, Kang,Caixia Li,Yuhuan Ding
摘要
The comprehension of bubble formation mechanisms in viscoelastic fluids within microchannels is crucial for the optimization of gas–liquid microreactions and microfluidic processes. In this study, a three-dimensional numerical investigation of bubble formation in viscoelastic fluids within a focusing microchannel was conducted using OpenFOAM. The volume of fluid method was employed to track the gas–liquid interface, while the Oldroyd-B model was utilized to describe the complex rheological behavior of the viscoelastic fluids. The effects of two-phase flow velocity ratio, relaxation time, and liquid viscosity on the evolution of the bubble neck width, bubble size, and channel pressure were observed. A model was proposed to characterize the evolution of the bubble neck width. Furthermore, an empirical correlation for predicting bubble size was proposed, with the relaxation time as a critical parameter based on dimensional analysis. The results revealed four flow patterns, including bubble flow, slug flow, tip-streaming, and annular flow. A flow pattern map was constructed based on two-phase velocities. Notably, the pressure drop within the main channel was significantly reduced by the viscoelastic property of the fluids, offering novel insights into the fluid dynamics of viscoelastic fluids at the microscale.
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