{"title":"涉及焦炭沉积的催化剂颗粒沉降的粒子分解晶格玻尔兹曼模拟","authors":"Yiqi Song , Xue Li , Mao Ye , Zhongmin Liu","doi":"10.1016/j.ces.2025.122129","DOIUrl":null,"url":null,"abstract":"<div><div>Catalyst deactivation by coke deposition in heterogeneous catalysis critically impacts reaction kinetics, yet its effects on particulate flows remain poorly understood. This work employs a particle-resolved immersed boundary-lattice Boltzmann method to analyze coke-influenced particle motion and particle–fluid interaction during sedimentation. The results reveal that for single/multiple particles, coke deposition on the catalyst particles gradually increases the particle density and accelerates the settling velocity of particles. When the reaction rate increases to certain extent, there exists a critical particle Reynolds number beyond which the vortex shedding around the catalyst appears, leading to a significant change in the flow pattern and particles motion. For settling of multiple particles, the initial release positions affect the movement of particles. Moreover, by analyzing the change of coke deposition rate during sedimentation, it is proved that the deactivation of catalyst is heterogeneous, which is caused by the uneven concentration distribution.</div></div>","PeriodicalId":271,"journal":{"name":"Chemical Engineering Science","volume":"317 ","pages":"Article 122129"},"PeriodicalIF":4.3000,"publicationDate":"2025-06-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Particle-resolved lattice Boltzmann simulations for sedimentation of catalyst particles involving coke deposition\",\"authors\":\"Yiqi Song , Xue Li , Mao Ye , Zhongmin Liu\",\"doi\":\"10.1016/j.ces.2025.122129\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>Catalyst deactivation by coke deposition in heterogeneous catalysis critically impacts reaction kinetics, yet its effects on particulate flows remain poorly understood. This work employs a particle-resolved immersed boundary-lattice Boltzmann method to analyze coke-influenced particle motion and particle–fluid interaction during sedimentation. The results reveal that for single/multiple particles, coke deposition on the catalyst particles gradually increases the particle density and accelerates the settling velocity of particles. When the reaction rate increases to certain extent, there exists a critical particle Reynolds number beyond which the vortex shedding around the catalyst appears, leading to a significant change in the flow pattern and particles motion. For settling of multiple particles, the initial release positions affect the movement of particles. Moreover, by analyzing the change of coke deposition rate during sedimentation, it is proved that the deactivation of catalyst is heterogeneous, which is caused by the uneven concentration distribution.</div></div>\",\"PeriodicalId\":271,\"journal\":{\"name\":\"Chemical Engineering Science\",\"volume\":\"317 \",\"pages\":\"Article 122129\"},\"PeriodicalIF\":4.3000,\"publicationDate\":\"2025-06-29\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering Science\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0009250925009522\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Science","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0009250925009522","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Particle-resolved lattice Boltzmann simulations for sedimentation of catalyst particles involving coke deposition
Catalyst deactivation by coke deposition in heterogeneous catalysis critically impacts reaction kinetics, yet its effects on particulate flows remain poorly understood. This work employs a particle-resolved immersed boundary-lattice Boltzmann method to analyze coke-influenced particle motion and particle–fluid interaction during sedimentation. The results reveal that for single/multiple particles, coke deposition on the catalyst particles gradually increases the particle density and accelerates the settling velocity of particles. When the reaction rate increases to certain extent, there exists a critical particle Reynolds number beyond which the vortex shedding around the catalyst appears, leading to a significant change in the flow pattern and particles motion. For settling of multiple particles, the initial release positions affect the movement of particles. Moreover, by analyzing the change of coke deposition rate during sedimentation, it is proved that the deactivation of catalyst is heterogeneous, which is caused by the uneven concentration distribution.
期刊介绍:
Chemical engineering enables the transformation of natural resources and energy into useful products for society. It draws on and applies natural sciences, mathematics and economics, and has developed fundamental engineering science that underpins the discipline.
Chemical Engineering Science (CES) has been publishing papers on the fundamentals of chemical engineering since 1951. CES is the platform where the most significant advances in the discipline have ever since been published. Chemical Engineering Science has accompanied and sustained chemical engineering through its development into the vibrant and broad scientific discipline it is today.