Hydrodynamics of gas-liquid microfluidics: A review

被引：25

作者：

Sheng, Lin ^{[1
]}

Chang, Yu ^{[1
]}

Wang, Junjie ^{[1
]}

Deng, Jian ^{[1
]}

Luo, Guangsheng ^{[1
]}

机构：

[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 10084, Peoples R China

来源：

CHEMICAL ENGINEERING SCIENCE | 2024年 / 285卷

基金：

中国国家自然科学基金;

关键词：

Microfluidics; Bubble size; Microdispersion; Microflow; Hydrodynamics; MASS-TRANSFER PERFORMANCE; 2-PHASE PRESSURE-DROP; BUBBLE FORMATION; T-JUNCTION; TAYLOR FLOW; SLUG FLOW; PART I; MICROCHEMICAL SYSTEMS; PARALLEL MICROCHANNEL; CARBON-DIOXIDE;

D O I：

10.1016/j.ces.2023.119563

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Gas-liquid multiphase process occupies a significant part in the chemical industry, and the emerging gas-liquid microfluidic technology provides a highly efficient and controllable tool for gas-liquid systems such as chemical product synthesis, gas separation, and environmental protection. To point out the microscale gas-liquid multi-phase process from the fundamental study to its utilization, this review mainly focuses on advances in the hy-drodynamics of the gas-liquid microdispersion and microflow for the design of the gas-liquid microfluidic device. The progress of the gas-liquid flow pattern is first introduced, and then the microdispersion in both single-channel and multi-channel are summarized from the bubble size prediction model and operating condi-tions. Besides, the microflow characteristic of bubble movement velocity and pressure drop in a single-channel and flow distribution in multi-channels for scaling-up are presented, and the design procedure of gas-liquid microreactors is proposed. Finally, a summary and perspective are provided.

引用

页数：20

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