Qiuwen Zhong, Zhen Jiao, Wenhui Nie, Yan Li, Ning Gu
{"title":"微通道内气液两相Taylor流传质行为的体积-流体多相流系统数值研究","authors":"Qiuwen Zhong, Zhen Jiao, Wenhui Nie, Yan Li, Ning Gu","doi":"10.1002/msd2.12049","DOIUrl":null,"url":null,"abstract":"<p>The microchannel reactor is the most commonly used microreaction technology, an innovative reaction system developed in recent years. This study investigates the mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by coupling the volume-of-fluid model and the species transport model. The concentration distribution and the volumetric mass transfer coefficient of the gas solute are determined and discussed in detail. The simulation results reveal that the double-circulation flow influences the concentration distribution in the liquid slug. The highest value is observed at the bubble's surface and decreases rapidly along the vertical direction of the bubble. The increase of bubble velocity leads to a more apparent decreasing trend. The gas–liquid interface renewal rate of the bubble is accelerated with increasing bubble velocity, resulting in an increase in the average mass transfer rate in all regions of the bubble surface with an increase in bubble velocity. The results also indicate that the liquid film area contributes the most to the mass transfer behavior due to the most significant proportion and average mass transfer rate of the liquid film among the bubble.</p>","PeriodicalId":60486,"journal":{"name":"国际机械系统动力学学报(英文)","volume":"2 3","pages":"253-264"},"PeriodicalIF":3.4000,"publicationDate":"2022-09-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://onlinelibrary.wiley.com/doi/epdf/10.1002/msd2.12049","citationCount":"1","resultStr":"{\"title\":\"Numerical investigation of mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by a volume-of-fluid multiphase flow system\",\"authors\":\"Qiuwen Zhong, Zhen Jiao, Wenhui Nie, Yan Li, Ning Gu\",\"doi\":\"10.1002/msd2.12049\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>The microchannel reactor is the most commonly used microreaction technology, an innovative reaction system developed in recent years. This study investigates the mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by coupling the volume-of-fluid model and the species transport model. The concentration distribution and the volumetric mass transfer coefficient of the gas solute are determined and discussed in detail. The simulation results reveal that the double-circulation flow influences the concentration distribution in the liquid slug. The highest value is observed at the bubble's surface and decreases rapidly along the vertical direction of the bubble. The increase of bubble velocity leads to a more apparent decreasing trend. The gas–liquid interface renewal rate of the bubble is accelerated with increasing bubble velocity, resulting in an increase in the average mass transfer rate in all regions of the bubble surface with an increase in bubble velocity. The results also indicate that the liquid film area contributes the most to the mass transfer behavior due to the most significant proportion and average mass transfer rate of the liquid film among the bubble.</p>\",\"PeriodicalId\":60486,\"journal\":{\"name\":\"国际机械系统动力学学报(英文)\",\"volume\":\"2 3\",\"pages\":\"253-264\"},\"PeriodicalIF\":3.4000,\"publicationDate\":\"2022-09-28\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://onlinelibrary.wiley.com/doi/epdf/10.1002/msd2.12049\",\"citationCount\":\"1\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"国际机械系统动力学学报(英文)\",\"FirstCategoryId\":\"1087\",\"ListUrlMain\":\"https://onlinelibrary.wiley.com/doi/10.1002/msd2.12049\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, MECHANICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"国际机械系统动力学学报(英文)","FirstCategoryId":"1087","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/msd2.12049","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, MECHANICAL","Score":null,"Total":0}
Numerical investigation of mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by a volume-of-fluid multiphase flow system
The microchannel reactor is the most commonly used microreaction technology, an innovative reaction system developed in recent years. This study investigates the mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by coupling the volume-of-fluid model and the species transport model. The concentration distribution and the volumetric mass transfer coefficient of the gas solute are determined and discussed in detail. The simulation results reveal that the double-circulation flow influences the concentration distribution in the liquid slug. The highest value is observed at the bubble's surface and decreases rapidly along the vertical direction of the bubble. The increase of bubble velocity leads to a more apparent decreasing trend. The gas–liquid interface renewal rate of the bubble is accelerated with increasing bubble velocity, resulting in an increase in the average mass transfer rate in all regions of the bubble surface with an increase in bubble velocity. The results also indicate that the liquid film area contributes the most to the mass transfer behavior due to the most significant proportion and average mass transfer rate of the liquid film among the bubble.