Chenyang Zhou , Weijin Liu , Yiming Xu , Jinbo Li , Bo Zhang
{"title":"微米尺度复合致密介质气固流化床床层密度波动特性的非线性分析","authors":"Chenyang Zhou , Weijin Liu , Yiming Xu , Jinbo Li , Bo Zhang","doi":"10.1016/j.cherd.2025.05.014","DOIUrl":null,"url":null,"abstract":"<div><div>This study proposes a Variational Mode Decomposition (VMD) method optimized by the Subtraction Average-Based Optimizer (SABO) and tailored for gas-solid fluidized beds, using the minimum permutation entropy as the fitness function. Combined with time-domain analysis and chaos analysis, the study systematically investigates the effects of varying ultrafine coal powder content on the stability of bed density fluctuations in micron-sized composite dense medium gas-solid fluidized beds. The research shows that adding a small fraction of ultrafine coal powder (<em>w</em>=1 %-<em>w</em>=3 %) suppresses the formation and coalescence of large bubbles and enhances operational predictability and stability. However, it can also promote channel blockage, leading to poor local fluidization and larger density fluctuations. A moderate amount of ultrafine coal powder (around <em>w</em>=6 %) significantly improves the uniformity of gas-solid distribution, reduces density fluctuations, thereby optimizing coal separation efficiency and precision. Conversely, an excessive dosage (<em>w</em>=8 % and above) increases system complexity and chaos, introducing new forms of instability. These results provide valuable theoretical guidance and practical recommendations for the design and operation of gas–solid fluidized beds, particularly in dry coal-separation applications.</div></div>","PeriodicalId":10019,"journal":{"name":"Chemical Engineering Research & Design","volume":"218 ","pages":"Pages 408-420"},"PeriodicalIF":3.7000,"publicationDate":"2025-05-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Nonlinear analysis of bed density fluctuation characteristics in gas-solid fluidized bed using micron-scale composite dense medium\",\"authors\":\"Chenyang Zhou , Weijin Liu , Yiming Xu , Jinbo Li , Bo Zhang\",\"doi\":\"10.1016/j.cherd.2025.05.014\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This study proposes a Variational Mode Decomposition (VMD) method optimized by the Subtraction Average-Based Optimizer (SABO) and tailored for gas-solid fluidized beds, using the minimum permutation entropy as the fitness function. Combined with time-domain analysis and chaos analysis, the study systematically investigates the effects of varying ultrafine coal powder content on the stability of bed density fluctuations in micron-sized composite dense medium gas-solid fluidized beds. The research shows that adding a small fraction of ultrafine coal powder (<em>w</em>=1 %-<em>w</em>=3 %) suppresses the formation and coalescence of large bubbles and enhances operational predictability and stability. However, it can also promote channel blockage, leading to poor local fluidization and larger density fluctuations. A moderate amount of ultrafine coal powder (around <em>w</em>=6 %) significantly improves the uniformity of gas-solid distribution, reduces density fluctuations, thereby optimizing coal separation efficiency and precision. Conversely, an excessive dosage (<em>w</em>=8 % and above) increases system complexity and chaos, introducing new forms of instability. These results provide valuable theoretical guidance and practical recommendations for the design and operation of gas–solid fluidized beds, particularly in dry coal-separation applications.</div></div>\",\"PeriodicalId\":10019,\"journal\":{\"name\":\"Chemical Engineering Research & Design\",\"volume\":\"218 \",\"pages\":\"Pages 408-420\"},\"PeriodicalIF\":3.7000,\"publicationDate\":\"2025-05-07\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering Research & Design\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0263876225002461\",\"RegionNum\":3,\"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 Research & Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0263876225002461","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Nonlinear analysis of bed density fluctuation characteristics in gas-solid fluidized bed using micron-scale composite dense medium
This study proposes a Variational Mode Decomposition (VMD) method optimized by the Subtraction Average-Based Optimizer (SABO) and tailored for gas-solid fluidized beds, using the minimum permutation entropy as the fitness function. Combined with time-domain analysis and chaos analysis, the study systematically investigates the effects of varying ultrafine coal powder content on the stability of bed density fluctuations in micron-sized composite dense medium gas-solid fluidized beds. The research shows that adding a small fraction of ultrafine coal powder (w=1 %-w=3 %) suppresses the formation and coalescence of large bubbles and enhances operational predictability and stability. However, it can also promote channel blockage, leading to poor local fluidization and larger density fluctuations. A moderate amount of ultrafine coal powder (around w=6 %) significantly improves the uniformity of gas-solid distribution, reduces density fluctuations, thereby optimizing coal separation efficiency and precision. Conversely, an excessive dosage (w=8 % and above) increases system complexity and chaos, introducing new forms of instability. These results provide valuable theoretical guidance and practical recommendations for the design and operation of gas–solid fluidized beds, particularly in dry coal-separation applications.
期刊介绍:
ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering.
Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.