{"title":"脂肪酸甲酯环氧化逆流接触旋流反应器涡特性数值模拟","authors":"Yaojun Guo, Mingyang Zhang, Yuanjing Liu, Wenjie Zhu, Jie Cheng, Haozhe Guo, Yingchun Yuan","doi":"10.1016/j.cep.2025.110475","DOIUrl":null,"url":null,"abstract":"<div><div>Using Eulerian model and RSM model, the vortex characteristics of the flow field with a counter flow contact-cyclone reactor for epoxidation of fatty acid methyl esters were analyzed. The impinging stream technology was used to optimize the mixing and reaction of FAME and performic acid. By varying the impingement distance (L<sub>1</sub>) and accelerator tube length (L<sub>2</sub>), the vorticity, swirling strength, and vortex kinetic energy distribution of the flow field were discussed using vorticity, normalized swirling strength standard deviation, and Q-criterion. Furthermore, the vortex core interaction range and evolution process in the reactor were studied based on the radial variations of vorticity and swirling strength standard deviation. Significantly, when L<sub>1</sub> = 40 mm and L<sub>2</sub> = 30 mm, the development of the vorticity reached the optimal working condition. Analysis of vorticity and Q-criterion isosurfaces indicates that small-scale vortices are distributed near the impingement chamber walls, while large-scale vortices are located at the impingement center. Notably, the vortex structures in the counter flow contact chamber are dominated by horseshoe and ribbed vortices. The evolution of vortices in the radial plane of the counter flow contact chamber is divided into four stages according to Q-criterion variations, and the flow field stabilizes after t = 0.18 s.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"217 ","pages":"Article 110475"},"PeriodicalIF":3.9000,"publicationDate":"2025-07-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Numerical of vortex characteristics in a counter flow contact-cyclone reactor for epoxidation of fatty acid methyl ester\",\"authors\":\"Yaojun Guo, Mingyang Zhang, Yuanjing Liu, Wenjie Zhu, Jie Cheng, Haozhe Guo, Yingchun Yuan\",\"doi\":\"10.1016/j.cep.2025.110475\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Using Eulerian model and RSM model, the vortex characteristics of the flow field with a counter flow contact-cyclone reactor for epoxidation of fatty acid methyl esters were analyzed. The impinging stream technology was used to optimize the mixing and reaction of FAME and performic acid. By varying the impingement distance (L<sub>1</sub>) and accelerator tube length (L<sub>2</sub>), the vorticity, swirling strength, and vortex kinetic energy distribution of the flow field were discussed using vorticity, normalized swirling strength standard deviation, and Q-criterion. Furthermore, the vortex core interaction range and evolution process in the reactor were studied based on the radial variations of vorticity and swirling strength standard deviation. Significantly, when L<sub>1</sub> = 40 mm and L<sub>2</sub> = 30 mm, the development of the vorticity reached the optimal working condition. Analysis of vorticity and Q-criterion isosurfaces indicates that small-scale vortices are distributed near the impingement chamber walls, while large-scale vortices are located at the impingement center. Notably, the vortex structures in the counter flow contact chamber are dominated by horseshoe and ribbed vortices. The evolution of vortices in the radial plane of the counter flow contact chamber is divided into four stages according to Q-criterion variations, and the flow field stabilizes after t = 0.18 s.</div></div>\",\"PeriodicalId\":9929,\"journal\":{\"name\":\"Chemical Engineering and Processing - Process Intensification\",\"volume\":\"217 \",\"pages\":\"Article 110475\"},\"PeriodicalIF\":3.9000,\"publicationDate\":\"2025-07-28\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering and Processing - Process Intensification\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S025527012500323X\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S025527012500323X","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
Numerical of vortex characteristics in a counter flow contact-cyclone reactor for epoxidation of fatty acid methyl ester
Using Eulerian model and RSM model, the vortex characteristics of the flow field with a counter flow contact-cyclone reactor for epoxidation of fatty acid methyl esters were analyzed. The impinging stream technology was used to optimize the mixing and reaction of FAME and performic acid. By varying the impingement distance (L1) and accelerator tube length (L2), the vorticity, swirling strength, and vortex kinetic energy distribution of the flow field were discussed using vorticity, normalized swirling strength standard deviation, and Q-criterion. Furthermore, the vortex core interaction range and evolution process in the reactor were studied based on the radial variations of vorticity and swirling strength standard deviation. Significantly, when L1 = 40 mm and L2 = 30 mm, the development of the vorticity reached the optimal working condition. Analysis of vorticity and Q-criterion isosurfaces indicates that small-scale vortices are distributed near the impingement chamber walls, while large-scale vortices are located at the impingement center. Notably, the vortex structures in the counter flow contact chamber are dominated by horseshoe and ribbed vortices. The evolution of vortices in the radial plane of the counter flow contact chamber is divided into four stages according to Q-criterion variations, and the flow field stabilizes after t = 0.18 s.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.